JPH0532902B2 - - Google Patents

Info

Publication number
JPH0532902B2
JPH0532902B2 JP63157701A JP15770188A JPH0532902B2 JP H0532902 B2 JPH0532902 B2 JP H0532902B2 JP 63157701 A JP63157701 A JP 63157701A JP 15770188 A JP15770188 A JP 15770188A JP H0532902 B2 JPH0532902 B2 JP H0532902B2
Authority
JP
Japan
Prior art keywords
wafer
heating section
heating
vapor phase
phase growth
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.)
Expired - Lifetime
Application number
JP63157701A
Other languages
Japanese (ja)
Other versions
JPH027419A (en
Inventor
Kichizo Komyama
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.)
Shibaura Machine Co Ltd
Original Assignee
Toshiba Machine Co 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 Toshiba Machine Co Ltd filed Critical Toshiba Machine Co Ltd
Priority to JP15770188A priority Critical patent/JPH027419A/en
Publication of JPH027419A publication Critical patent/JPH027419A/en
Publication of JPH0532902B2 publication Critical patent/JPH0532902B2/ja
Granted legal-status Critical Current

Links

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、気相成長装置に係り、特に気相成長
を施こされるウエハの均一加熱に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Application Field) The present invention relates to a vapor phase growth apparatus, and particularly to uniform heating of a wafer subjected to vapor phase growth.

(従来の技術) 従来の気相成長装置、特にエピタキシヤル気相
成長装置におけるウエハの加熱にはRF加熱と輻
射加熱とが用いられている。RF加熱はカーボン
製のサセプタ上にウエハを載置してサセプタを
RFコイルにより誘導加熱してウエハを裏面から
加熱するものであり、輻射加熱は同じくサセプタ
上にウエハを載置し、ウエハおよびサセプタの表
面側から赤外線ランプ等によつて輻射加熱するこ
とによりウエハを表面側から直接輻射加熱すると
共に裏面側からサセプタによつて加熱したり、特
公昭63−6627号のように赤外線を発する平行な2
枚の加熱板間にウエハを置いて表裏両面から直接
輻射加熱したりするものがある。
(Prior Art) RF heating and radiation heating are used to heat a wafer in a conventional vapor phase growth apparatus, particularly an epitaxial vapor phase growth apparatus. For RF heating, the wafer is placed on a carbon susceptor and the susceptor is heated.
The wafer is heated from the back side by induction heating using an RF coil, while the wafer is heated from the back side by radiant heating, which is done by placing the wafer on a susceptor and heating the wafer by radiation from the front side of the wafer and susceptor using an infrared lamp or the like. Direct radiation heating from the front side and heating from the back side with a susceptor, or parallel heating that emits infrared rays as in Japanese Patent Publication No. 63-6627.
There is a method in which the wafer is placed between two heating plates and is directly heated by radiation from both the front and back sides.

(発明が解決しようとする課題) 上記RF加熱は周知のようにウエハが裏面から
加熱されるために、特に表裏の温度差を生ずる欠
点があり、このため表面から輻射加熱を付加する
ことが行なわれている。上記特公昭63−6627号は
ウエハの表裏内面加熱をより均一に行なうことの
できるものであるが、これを用いられているよう
な平板状の加熱板は周辺部での放熱が大きいた
め、中央部より外周部の方が温度が低い傾向を示
す。そこで、加熱板の面積をウエハ載置部より相
当大きくする必要がある。特に、ウエハを一方の
加熱板上に間隔を置かずに実質的に接触させた状
態で載置する場合には、ウエハは加熱板の温度に
敏感に左右されるため、ウエハ載置部の温度をよ
り完全に均一にする必要性から該加熱板の面積を
より一層大きくする必要がある。
(Problem to be Solved by the Invention) As is well known, the above-mentioned RF heating has the drawback that the wafer is heated from the back side, which causes a temperature difference between the front and back sides.For this reason, radiant heating is applied from the front side. It is. The above-mentioned Japanese Patent Publication No. 63-6627 can heat the front and back surfaces of a wafer more uniformly, but the flat heating plate used in this method dissipates a lot of heat at the periphery, so The temperature tends to be lower at the outer periphery than at the outer periphery. Therefore, it is necessary to make the area of the heating plate considerably larger than the wafer placement part. In particular, when wafers are placed on one heating plate in a state where they are substantially in contact with each other without leaving any space between them, the wafer is sensitive to the temperature of the heating plate, so the temperature of the wafer placement area Because of the need to make the temperature more completely uniform, it is necessary to further increase the area of the heating plate.

本発明は、より小型の装置でウエハの均一加熱
を達成することのできる気相成長装置を提供する
ことを目的とするものである。
An object of the present invention is to provide a vapor phase growth apparatus that can achieve uniform heating of a wafer with a smaller apparatus.

〔発明の構成〕[Structure of the invention]

(課題を解決するための手段) 上記目的を達成するための本発明の気相成長装
置は、反応室の外壁を強制冷却するコールドウオ
ール式の気相成長装置において、反応室内に配置
され一方をガス導入側とし他方を排気側とする開
口を有し内部にウエハを直接または間接的に載置
する偏平な筒状の加熱部と、この加熱部の全外周
面を加熱するように反応室外に設けられた輻射加
熱手段とを備え、少なくとも加熱部内に反応ガス
を流すようにしたものである。
(Means for Solving the Problems) A vapor phase growth apparatus of the present invention for achieving the above object is a cold wall type vapor growth apparatus that forcibly cools the outer wall of the reaction chamber. A flat cylindrical heating section has an opening on the gas inlet side and the other side as the exhaust side, in which the wafer is directly or indirectly placed, and a heating section outside the reaction chamber that heats the entire outer peripheral surface of this heating section. A radiation heating means is provided, and a reaction gas is caused to flow through at least the heating section.

加熱部は、実質的に偏平な角筒状とし、輻射加
熱手段を角筒状の外周4面にそれぞれ対応して設
けることが好ましい。
Preferably, the heating section has a substantially flat rectangular tube shape, and radiation heating means are provided corresponding to each of the four outer peripheral surfaces of the rectangular tube shape.

また、加熱部内におけるウエハの載置は、通常
の気相成長装置においてウエハをサセプタ上に載
置するのと同様にウエハを加熱部内壁上に載置す
るようにしてもよいし、また加熱部内に別に支持
部材を設けてこの上に載置してもよく、さらにま
たウエハの表裏両面の外周近くを除く大部分ない
し全体を加熱部の対向する2面の内壁に対しそれ
ぞれ間隔を置いて対向させるように載置してもよ
い。
Furthermore, the wafer may be placed on the inner wall of the heating section in the same way as the wafer is placed on a susceptor in a normal vapor phase growth apparatus, or the wafer may be placed on the inner wall of the heating section. A support member may be provided separately for the wafer and the wafer may be placed on the support member.Furthermore, most or all of the wafer, except for the vicinity of the outer periphery, on both the front and back sides of the wafer may be placed so as to face the two opposing inner walls of the heating section at a distance from each other. It may also be placed so that it

(作 用) ウエハは、偏平な筒状の加熱部内に載置され、
加熱部の内壁からの熱伝導と輻射による加熱また
は実質的に輻射のみによる加熱を表裏および周囲
から受ける。このとき、加熱部はウエハの表裏に
対応する外周面部分のみなならず側方部分をも含
む実質的に全外周面を加熱されるため、加熱部内
部は中央から端部までより均一な温度となり、該
加熱部の内部空間の特にガス流と直交する方向の
幅をウエハの直径に近付けてもウエハ全体を高精
度で均一に加熱する。
(Function) The wafer is placed in a flat cylindrical heating section,
The heating section receives heating by heat conduction and radiation from the inner wall of the heating section, or heating by substantially only radiation from the front and back and the surroundings. At this time, the heating section heats substantially the entire outer circumferential surface of the wafer, including not only the outer circumferential surface portions corresponding to the front and back sides of the wafer, but also the side portions, so the temperature inside the heating section is more uniform from the center to the edges. Therefore, even if the width of the internal space of the heating section, particularly in the direction perpendicular to the gas flow, is made close to the diameter of the wafer, the entire wafer can be heated uniformly with high precision.

加熱部内部空間の高さは、できるだけ小さな寸
法であることが好ましく、これにより加熱効率が
高まると共にウエハ温度が安定し、さらに反応室
全体の断面積を小さくできるため、ガスの有効利
用と使用量の低減が図られる。
It is preferable that the height of the internal space of the heating section is as small as possible. This increases heating efficiency and stabilizes the wafer temperature. Furthermore, since the cross-sectional area of the entire reaction chamber can be reduced, the effective use of gas and the amount used can be achieved. This will result in a reduction in

(実施例) 以下本発明の一実施例を示す第1図および第2
図をを参照して説明する。11は、反応室10を
形成する石英ガラス製の反応容器で、横断面形状
が第2図に示すように偏平角筒状をしており、第
1図において左端のフランジ部11aを締付け板
12で締付けることにより装置フレーム13に固
定されている。
(Example) The following Figures 1 and 2 show an example of the present invention.
This will be explained with reference to the figure. Reference numeral 11 denotes a reaction vessel made of quartz glass that forms the reaction chamber 10, and its cross-sectional shape is a flat rectangular cylinder as shown in FIG. 2. In FIG. It is fixed to the device frame 13 by tightening with.

締付け板12には、反応容器11の内壁と略一
致する穴12aが明けられ、この穴12aにステ
ンレス鋼製のガス供給部材14が嵌着されてい
る。ガス供給部材14の中央には、反応ガスおよ
びパージガスを供給するための偏平な段付き穴1
5が明けられると共に、締付け板12との係合部
外周にはパージガスを供給するための環状溝16
が設けられている。前記段付き穴15および環状
溝16には、締付け板12に設けた流路17,1
8を介して第1、第2配管19,20から反応ガ
スまたはパージガスが供給されるようになつてい
る。
A hole 12a that substantially coincides with the inner wall of the reaction vessel 11 is formed in the clamping plate 12, and a gas supply member 14 made of stainless steel is fitted into this hole 12a. In the center of the gas supply member 14, there is a flat stepped hole 1 for supplying reaction gas and purge gas.
5 is opened, and an annular groove 16 for supplying purge gas is formed on the outer periphery of the engagement portion with the tightening plate 12.
is provided. The stepped hole 15 and the annular groove 16 are provided with channels 17 and 1 provided in the tightening plate 12.
Reactant gas or purge gas is supplied from first and second pipes 19 and 20 via pipe 8 .

締付け板12の第1図において左端には、フタ
21が着脱可能に取付けられ、このフタ21によ
つて前記段付き穴15の左端側を密閉するように
なつている。フタ21には、段付き穴15の段部
に対応すべく複数本のロツド22を介して整流板
23が取付けられている。この整流板23は多数
の小孔を有するパンチメタル状のものである。
A lid 21 is removably attached to the left end of the tightening plate 12 in FIG. 1, and the lid 21 seals the left end of the stepped hole 15. A rectifying plate 23 is attached to the lid 21 via a plurality of rods 22 so as to correspond to the stepped portion of the stepped hole 15. This rectifying plate 23 is a punched metal type having a large number of small holes.

段付き穴15の第1図において右端には、石英
ガラス製の偏平なガス導入管24が接続されてい
る。また、ガス供給部材14には、環状溝16を
反応室10の内壁とガス導入管24の外周との間
の空間に接続させる多数のガス導入口25が明け
られている。
A flat gas introduction pipe 24 made of quartz glass is connected to the right end of the stepped hole 15 in FIG. Further, the gas supply member 14 is provided with a large number of gas introduction ports 25 that connect the annular groove 16 to the space between the inner wall of the reaction chamber 10 and the outer periphery of the gas introduction pipe 24 .

反応室10内には、カーボン製で表面にSiCコ
ートを施こした加熱部26が石英ガラス製のトレ
イ27を介して設置されている。この加熱部26
は、第1図において左右方向に伸びる断面状
(第2図参照)の下加熱体26aと、この上にか
ぶせられる上加熱体26bとからなり、全体とし
て偏平な角筒状をし、底面上にウエハWを載置す
るようになつている。なお、この加熱部26は一
体形成してもよいし、また上下左右に4分割して
もよいなど、適宜に形成できる。この加熱部26
は、上加熱体26bが水平であるとき、下加熱体
26aの底壁は第1図において左より右が2゜程度
高くなるように勾配を付与されている。加熱部2
6の第1図において左側の開口は、上記ガス導入
管24に若干すき間を有するように接続され、右
側の開口は、反応容器11の右端の排気口28に
向けて開放されている。ここに、前記段付き穴1
5、ガス導入管24ならびに加熱部26の内部横
断面形状は略一致するように形成されている。
Inside the reaction chamber 10, a heating section 26 made of carbon and coated with SiC on the surface is installed via a tray 27 made of quartz glass. This heating section 26
consists of a lower heating element 26a with a cross-sectional shape extending in the left-right direction in FIG. The wafer W is placed on the wafer W. Note that this heating section 26 may be formed in any suitable manner, such as being integrally formed or divided into four parts vertically, horizontally, and horizontally. This heating section 26
In FIG. 1, when the upper heating element 26b is horizontal, the bottom wall of the lower heating element 26a is sloped so that the right side is about 2 degrees higher than the left side in FIG. Heating section 2
6, the opening on the left side is connected to the gas introduction pipe 24 with a slight gap, and the opening on the right side is open toward the exhaust port 28 at the right end of the reaction vessel 11. Here, the stepped hole 1
5. The internal cross-sectional shapes of the gas introduction pipe 24 and the heating section 26 are formed to substantially match each other.

反応容器11の周囲はカバー29で被われ、そ
の内部の加熱部26に対向する部分に輻射加熱手
段30,31,32,33(第2図参照)が設け
られている。第1,2図において、上下に位置す
る輻射加熱手段30,31は加熱部26の上下の
外周面に対向し、棒状の赤外線ランプ34を第2
図において左右方向に向け、第1図において左右
方向に間隔を置いて複数本配列されている。これ
らの複数本の赤外線ランプ34は第1図におい
て、2本づつ左、中央、右に3区分されて出力調
整可能になされている。また、第2図において、
加熱部26の左右の外周面に対向している輻射加
熱手段32,33は、棒状の赤外線ランプ34を
左右の外周面の長手方向に沿うように取付けられ
ている。
The periphery of the reaction vessel 11 is covered with a cover 29, and radiation heating means 30, 31, 32, 33 (see FIG. 2) are provided inside the cover 29 at a portion facing the heating section 26. In FIGS. 1 and 2, the radiant heating means 30 and 31 located above and below face the upper and lower outer peripheral surfaces of the heating section 26, and a rod-shaped infrared lamp 34 is connected to the second
A plurality of them are arranged at intervals in the left-right direction in the figure, and in the left-right direction in FIG. In FIG. 1, these plurality of infrared lamps 34 are divided into three sections, two each on the left, center, and right, so that their output can be adjusted. Also, in Figure 2,
Radiation heating means 32 and 33 facing the left and right outer peripheral surfaces of the heating section 26 have rod-shaped infrared lamps 34 attached along the longitudinal direction of the left and right outer peripheral surfaces.

それぞれの赤外線ランプ34は反射と冷却機能
を有するランプハウジング35にそれぞれ取付け
られており、各供給ポート36から冷却空気を供
給され、ランプハウジング35、赤外線ランプ3
4および反応容器11を冷却するようになつてい
る。また、カバー29の第1図において右端寄り
にも供給ポート37が設けられ、冷却空気をカバ
ー29内すなわち反応容器11の周囲に供給する
ようになつている。なお、第1図においてカバー
29の左端寄りには排気ポート38が設けられて
いる。
Each infrared lamp 34 is attached to a lamp housing 35 having a reflection and cooling function, and is supplied with cooling air from each supply port 36.
4 and reaction vessel 11. Further, a supply port 37 is provided near the right end of the cover 29 in FIG. 1 to supply cooling air into the cover 29, that is, around the reaction vessel 11. Note that in FIG. 1, an exhaust port 38 is provided near the left end of the cover 29.

次いで本装置の作用について説明する。ウエハ
Wの搬出入は、フタ21を外して行なう。フタ2
1を外すことにより段付き穴15の段部にあつた
整流板23が外され、段付き穴15、ガス導入管
24を介して加熱部26の内部空間が第1図にお
いて左端側に開放される。そこで、段付き穴15
側から図示しない搬送装置によりウエハWの搬出
入を行なう。
Next, the operation of this device will be explained. The wafer W is carried in and out by removing the lid 21. Lid 2
1, the rectifying plate 23 located at the step of the stepped hole 15 is removed, and the internal space of the heating section 26 is opened to the left end side in FIG. 1 through the stepped hole 15 and the gas introduction pipe 24. Ru. Therefore, stepped hole 15
The wafer W is loaded and unloaded from the side by a transport device (not shown).

ウエハWを搬入したならば、第1、第2配管1
9,20から共にN2ガス、H2ガス等のパージガ
スを供給し、輻射加熱手段30〜33によつて昇
温を開始する。この加熱において、加熱部26の
第1図において左右(長手)方向の温度分布は、
輻射加熱手段30,31の各赤外線ランプ34の
出力を左、中央、右の各区分毎に調整することに
よつて均一化し、他方、加熱部26の第2図にお
いて左右(幅)方向の温度分布は、輻射加熱手段
32,33の出力を調整することによつて均一に
なされる。また、第1,2図に示すように、ウエ
ハWを加熱部26の底壁上に直接載置する場合に
は、ウエハWの裏面は実質的に熱伝導によつて加
熱され、表面は加熱部26の上内壁からの輻射に
よつて加熱されるため、上下の輻射加熱手段3
0,31の出力を独立して調整し、ウエハWの表
裏の温度差をより小さく押えることが好ましい。
なお、左右の輻射加熱手段32,33も別々出力
を調整できるようにしておくことが好ましい。
After loading the wafer W, the first and second pipes 1
Purge gas such as N 2 gas and H 2 gas is supplied from 9 and 20, and temperature rise is started by the radiant heating means 30 to 33. In this heating, the temperature distribution in the left and right (longitudinal) direction in FIG. 1 of the heating section 26 is as follows:
The output of each infrared lamp 34 of the radiant heating means 30, 31 is adjusted for each section on the left, center, and right to make it uniform, and on the other hand, the temperature of the heating section 26 in the left and right (width) direction in FIG. The distribution is made uniform by adjusting the output of the radiant heating means 32, 33. In addition, as shown in FIGS. 1 and 2, when the wafer W is placed directly on the bottom wall of the heating section 26, the back surface of the wafer W is substantially heated by thermal conduction, and the front surface is heated. Since it is heated by radiation from the upper inner wall of the section 26, the upper and lower radiation heating means 3
It is preferable to adjust the outputs of 0 and 31 independently to suppress the temperature difference between the front and back sides of the wafer W.
Note that it is preferable that the outputs of the left and right radiant heating means 32 and 33 can also be adjusted separately.

加熱部26が気相成長温度に達したならば、
H2ガスに変えて反応ガスを第1配管19から供
給し、段付き穴15、整流板26、ガス導入管2
4を介して加熱部26内に層流で反応ガスを流し
て、ウエハWの表面に気相成長を行なう。他方、
第2配管18からはパージガスとしてのH2ガス
を供給し続け、反応ガスが直接反応容器11の内
壁に接触することを極力防止する。なお、ガス供
給部材14および加熱部26とガス導入管24と
の接続は、熱膨脹の関係などから若干すき間を有
するように形成されているため、この接続部から
反応ガスが漏れ出すが、その量はわずかであり、
反応容器11の内壁に沿つてパージガスが流れて
いるため、反応容器11の内壁にウオールデポを
生じることはほとんどない。
Once the heating section 26 reaches the vapor phase growth temperature,
Reactant gas is supplied from the first pipe 19 instead of H 2 gas, and the stepped hole 15, the rectifier plate 26, and the gas introduction pipe 2
A reactant gas is caused to flow in a laminar flow into the heating section 26 through the wafer W to perform vapor phase growth on the surface of the wafer W. On the other hand,
H 2 gas as a purge gas is continuously supplied from the second pipe 18 to prevent the reaction gas from directly contacting the inner wall of the reaction vessel 11 as much as possible. Note that the connections between the gas supply member 14 and the heating section 26 and the gas introduction pipe 24 are formed with a slight gap due to thermal expansion, so the reaction gas leaks from these connections, but the amount is limited. is small,
Since the purge gas flows along the inner wall of the reaction vessel 11, wall deposits are hardly generated on the inner wall of the reaction vessel 11.

前記加熱部26内を流れる反応ガスによる気相
成長は、加熱部26の内部空間が比較的狭く囲ま
れ、均一な温度分布になされているため、ウエハ
Wは全体がより均一に加熱され、スリツプを生じ
ないと共に膜厚分布も均一になり、かつより少な
い反応ガスによつて効率のよい気相成長が行なわ
れる。また、加熱部26の断面形状の小形化によ
り反応容器11の断面形状も小形になり、そのた
め、第2配管20から供給するパージガスの流量
も少なくできる。
In the vapor phase growth using the reaction gas flowing inside the heating section 26, the interior space of the heating section 26 is surrounded by a relatively narrow space and has a uniform temperature distribution, so that the entire wafer W is heated more uniformly and slips. In addition, the film thickness distribution becomes uniform, and efficient vapor phase growth is performed using less reaction gas. Further, by making the cross-sectional shape of the heating section 26 smaller, the cross-sectional shape of the reaction vessel 11 is also made smaller, and therefore, the flow rate of the purge gas supplied from the second pipe 20 can also be reduced.

第3図は、本発明の他の実施例の要部を示すも
ので、加熱部26の内部空間の高さを低くし、か
つ底面にはウエハWの外周付近のみを支持する浅
い段部40を有する深いザグリ41を設け、ウエ
ハWの表裏両面ほぼ全体を輻射によつて加熱する
ようにしたものである。また、この実施例では、
ガス導入管24を加熱部26の左端外周に若干す
き間を持たせて係合させたものである。この実施
例によれば、ウエハWの表面両面が共に輻射加熱
されるため、容易にウエハWの均一加熱が可能で
ある。
FIG. 3 shows the main part of another embodiment of the present invention, in which the height of the internal space of the heating section 26 is reduced, and a shallow stepped portion 40 on the bottom surface supports only the vicinity of the outer periphery of the wafer W. A deep counterbore 41 is provided so that substantially the entire front and back surfaces of the wafer W are heated by radiation. Also, in this example,
The gas introduction pipe 24 is engaged with the outer periphery of the left end of the heating section 26 with a slight gap. According to this embodiment, since both surfaces of the wafer W are heated by radiation, the wafer W can be easily heated uniformly.

第4図は、本発明のさらに他の実施例の要部を
示すもので、加熱部26内にSiCコーテイングし
たカーボンまたは石英ガラス製の支持部材42を
設け、この上にウエハWを載置したもので、これ
によつても第1,2図に示した実施例と同様の気
相成長を行なうことができる。
FIG. 4 shows a main part of still another embodiment of the present invention, in which a support member 42 made of SiC-coated carbon or quartz glass is provided in the heating section 26, and a wafer W is placed on this support member 42. With this method, the same vapor phase growth as in the embodiment shown in FIGS. 1 and 2 can be performed.

前述した実施例は、ガス導入管24を石英ガラ
ス製として例を示したがSiCコーテイングしたカ
ーボン製としてもよい。なお、このガス導入管2
4は第5図に示すように省略してもよい。この場
合は反応容器11をより強く冷却することにより
ウオールデポを押えることができる。またこの実
施例においては、支持部材42または加熱部26
を反応容器11外へ搬出してウエハWの搬出入を
行なうことが可能となる。
In the above embodiment, the gas introduction tube 24 is made of quartz glass, but it may be made of carbon coated with SiC. Note that this gas introduction pipe 2
4 may be omitted as shown in FIG. In this case, the wall deposit can be suppressed by cooling the reaction vessel 11 more strongly. Further, in this embodiment, the supporting member 42 or the heating section 26
The wafer W can be carried in and out by carrying it out of the reaction vessel 11.

また、加熱部26と排気口28の間に図示しな
いガス導出管を置き、ガスの乱れをより確実に押
えるようにしてもよい。さらにまた、熱部26は
必ずしも水平である必要はなく、長手方向または
幅方向を上下にして立ててもよく、またウエハW
の載置は上記実施例のほかに、加熱部26の底面
上に石英ガラスやSiCコーテイングカーボン製の
リングを置くことにより、ウエハWの表裏両面の
外周近くを除く大部分ないし全体が加熱部26の
対向する2面の内壁に対しそれぞれ間隔を置いて
対向するようにし、第3図に示した実施例と同様
に表裏両面を伝導によらずに輻射加熱するように
してもよい。
Furthermore, a gas outlet pipe (not shown) may be placed between the heating section 26 and the exhaust port 28 to more reliably suppress gas turbulence. Furthermore, the heating section 26 does not necessarily have to be horizontal, and may be erected with its longitudinal direction or width direction up and down, and the wafer W
In addition to the above embodiment, the wafer W can be placed on the heating section 26 by placing a ring made of quartz glass or SiC coated carbon on the bottom surface of the heating section 26, so that most or the entire wafer W is placed on the heating section 26, except for the vicinity of the outer periphery of both the front and back surfaces of the wafer W. They may be arranged to face the inner walls of the two opposing sides at a distance from each other, and both the front and back surfaces may be heated by radiation instead of by conduction, as in the embodiment shown in FIG.

次に、上記第1図および第2図に示した装置に
よる実験結果を示す。加熱部26のガス導入側の
外形寸法を幅212mm、高さ30mm、長さ230mmで各壁
の厚さ6mmとし、ガス排気側に向つて底面が2゜高
くなるようにした。底面にはウエハWを載置する
ザグリを1つ設け、この中に6インチのSiウエハ
Wを1枚載置した。赤外線ランプ34は、第2図
において上下を各6本、左右を各1本とし、加熱
部26の内壁の温度を熱電対で測定しつつ前記赤
外線ランプ34の出力調整を行なつて、1100℃に
加熱した。この結果、加熱部26の長手方向およ
び幅方向のいずれにおいてもほぼ全体にわたつて
均一な温度分布が得られた。
Next, experimental results using the apparatus shown in FIGS. 1 and 2 above will be shown. The external dimensions of the gas introduction side of the heating section 26 were 212 mm in width, 30 mm in height, and 230 mm in length, with each wall having a thickness of 6 mm, and the bottom surface was raised by 2° toward the gas exhaust side. One counterbore for placing a wafer W was provided on the bottom surface, and one 6-inch Si wafer W was placed in this counterbore. The infrared lamps 34 have six infrared lamps each on the top and bottom and one each on the left and right in FIG. heated to. As a result, a uniform temperature distribution was obtained over almost the entire heating section 26 in both the longitudinal direction and the width direction.

また、上記加熱状態において、第1配管19か
らSiH2Cl2B:H2が0.5:100の反応ガスを20/
minで供給すると共に、第2配管20からH2
スを10/minで供給して気相成長を行なつた結
果、膜成長速度は約1μ/min、膜厚分布誤差は約
2%であり、スリツプは肉眼検査はもちろん顕微
鏡検査でも見られなかつた。
In addition, in the above heating state, a reaction gas containing SiH 2 Cl 2 B:H 2 of 0.5:100 is supplied from the first pipe 19 at a ratio of 20/20.
As a result, the film growth rate was approximately 1 μ/min, and the film thickness distribution error was approximately 2%. , the slip was not seen by macroscopic or microscopic examination.

さらにまた、反応容器11には、ウオールデポ
を全く生じず、ガス導入管24の加熱部26寄り
に若干ウオールデポを生じた程度であつた。
Furthermore, no wall deposits were formed in the reaction vessel 11, and only some wall deposits were formed near the heating section 26 of the gas introduction pipe 24.

〔発明の効果〕〔Effect of the invention〕

以上述べたように本発明によれば、小型の装置
で6インチウエハのような比較的大径のウエハに
対し高品位の気相成長を行なうことができ、装置
の小形化により加熱ウエネルギやガス使用量を低
く押えてランニングコストを下げることができ
る。なお、加熱部を実質的に偏平な角筒状とすれ
ば幅方向のガス流量の均一性を阻害することなく
加熱部をより薄くして加熱効率を高めることがで
きる。また、実質的に角筒状の場合は外周4面に
それぞれ対応して輻射加熱手段を設けることによ
つて加熱部の幅方向の温度分布を均一化できる。
さらにまた、ウエハは加熱部に直接または間接の
いずれによつて載置してもよいが、ウエハの表裏
両面の外周近くを除く大部分ないし全体が加熱部
内壁に対して間隔を有するようにすれば、表裏の
温度差をより小さくできる。
As described above, according to the present invention, high-quality vapor phase growth can be performed on relatively large diameter wafers such as 6-inch wafers using a small device, and the miniaturization of the device requires less heating energy and gas. It is possible to keep the amount used low and reduce running costs. Note that if the heating section is formed into a substantially flat rectangular tube shape, the heating efficiency can be increased by making the heating section thinner without impairing the uniformity of the gas flow rate in the width direction. Further, in the case of a substantially rectangular cylindrical shape, the temperature distribution in the width direction of the heating section can be made uniform by providing radiation heating means corresponding to each of the four outer peripheral surfaces.
Furthermore, the wafer may be placed on the heating section either directly or indirectly, but most or all of the wafer, except for the vicinity of the outer periphery on both the front and back surfaces, should be placed at a distance from the inner wall of the heating section. For example, the temperature difference between the front and back sides can be made smaller.

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

第1図は本発明の一実施例を示す縦断面図、第
2図は第1図の−線による横断面図、第3図
ないし第5図は本発明のそれぞれ異なる他の実施
例を示す要部縦断面図である。 10……反応室、11……反応容器、14……
ガス供給部材、23……整流板、24……ガス導
入管、25……ガス導入口、26……加熱部、2
8……排気口、30,31,32,33……輻射
加熱手段、34……赤外線ランプ、42……支持
部材、W……ウエハ。
FIG. 1 is a longitudinal cross-sectional view showing one embodiment of the present invention, FIG. 2 is a cross-sectional view taken along the line - in FIG. 1, and FIGS. 3 to 5 show other different embodiments of the present invention. It is a longitudinal cross-sectional view of the main part. 10...Reaction chamber, 11...Reaction container, 14...
Gas supply member, 23... Current plate, 24... Gas introduction pipe, 25... Gas inlet, 26... Heating section, 2
8... Exhaust port, 30, 31, 32, 33... Radiation heating means, 34... Infrared lamp, 42... Support member, W... Wafer.

Claims (1)

【特許請求の範囲】 1 反応室の外壁を強制冷却するコールドウオー
ル式の気相成長装置において、反応室内に配置さ
れ一方をガス導入側とし他方を排気側とする開口
を有し内部にウエハを直接または間接的に載置す
る偏平な筒状の加熱部と、同加熱部の全外周面を
加熱するように前記反応室外に設けられた輻射加
熱手段とを備え、少なくとも前記加熱部内に反応
ガスを流すようにしたことを特徴とする気相成長
装置。 2 加熱部が偏平な角筒状であり、輻射加熱手段
が前記角筒状部の外周4面にそれぞれ対応して設
けられていることを特徴とする請求項1記載の気
相成長装置。 3 ウエハが加熱部の内壁上に直接載置されるよ
うになつていることを特徴とする請求項1または
2記載の気相成長装置。 4 加熱部内にウエハの支持部材が設けられてい
ることを特徴とする請求項1または2記載の気相
成長装置。 5 ウエハの表裏両面の外周近くを除く大部分な
いし全体が、加熱部の対向する2面の内壁に対し
それぞれ間隔を置いて対向するようにウエハを加
熱部内に載置するようになつていることを特徴と
する請求項1、2、3または4記載の気相成長装
置。
[Scope of Claims] 1. A cold wall type vapor phase growth apparatus that forcibly cools the outer wall of a reaction chamber, which is disposed inside the reaction chamber and has an opening with one side as a gas inlet side and the other side as an exhaust side, and a wafer inside. It is equipped with a flat cylindrical heating section placed directly or indirectly, and a radiation heating means provided outside the reaction chamber so as to heat the entire outer peripheral surface of the heating section, and at least a reaction gas is provided inside the heating section. A vapor phase growth apparatus characterized by being configured to flow. 2. The vapor phase growth apparatus according to claim 1, wherein the heating section has a flat rectangular tube shape, and radiation heating means are provided corresponding to four outer circumferential surfaces of the rectangular tube section. 3. The vapor phase growth apparatus according to claim 1 or 2, wherein the wafer is placed directly on the inner wall of the heating section. 4. The vapor phase growth apparatus according to claim 1 or 2, further comprising a wafer support member provided within the heating section. 5. The wafer is placed in the heating section so that most or all of the wafer, excluding the vicinity of the outer periphery, on both the front and back sides of the wafer faces the two opposing inner walls of the heating section with a distance between them. The vapor phase growth apparatus according to claim 1, 2, 3, or 4, characterized in that:
JP15770188A 1988-06-24 1988-06-24 Vapor growth apparatus Granted JPH027419A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15770188A JPH027419A (en) 1988-06-24 1988-06-24 Vapor growth apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15770188A JPH027419A (en) 1988-06-24 1988-06-24 Vapor growth apparatus

Publications (2)

Publication Number Publication Date
JPH027419A JPH027419A (en) 1990-01-11
JPH0532902B2 true JPH0532902B2 (en) 1993-05-18

Family

ID=15655489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15770188A Granted JPH027419A (en) 1988-06-24 1988-06-24 Vapor growth apparatus

Country Status (1)

Country Link
JP (1) JPH027419A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7279502B2 (en) 1999-04-30 2007-10-09 Cellgate, Inc. Polyamine analog conjugates and quinone conjugates as therapies for cancers and prostate diseases

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3474602B2 (en) * 1993-05-07 2003-12-08 住友電気工業株式会社 Superconducting conductor
JP3501828B2 (en) * 1993-10-21 2004-03-02 住友電気工業株式会社 Manufacturing method of oxide superconducting conductor
JPH1027759A (en) * 1996-07-11 1998-01-27 Seiko Epson Corp Heat treatment apparatus, reduced pressure CVD apparatus, and method of manufacturing thin film apparatus

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5130477A (en) * 1974-09-09 1976-03-15 Kokusai Electric Co Ltd KISOSEICHOSOCHI
JPS6054919B2 (en) * 1976-08-06 1985-12-02 株式会社日立製作所 low pressure reactor
JPS5842225A (en) * 1981-09-04 1983-03-11 Kokusai Electric Co Ltd Horizontal semiconductor vapor growth apparatus lising indirect heating
JPS5950093A (en) * 1982-09-10 1984-03-22 Toshiba Mach Co Ltd Diffusion furnace type vacuum vapor growth device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7279502B2 (en) 1999-04-30 2007-10-09 Cellgate, Inc. Polyamine analog conjugates and quinone conjugates as therapies for cancers and prostate diseases

Also Published As

Publication number Publication date
JPH027419A (en) 1990-01-11

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