JPS63199432A - Gas dispersing head for cvd device - Google Patents

Gas dispersing head for cvd device

Info

Publication number
JPS63199432A
JPS63199432A JP3285387A JP3285387A JPS63199432A JP S63199432 A JPS63199432 A JP S63199432A JP 3285387 A JP3285387 A JP 3285387A JP 3285387 A JP3285387 A JP 3285387A JP S63199432 A JPS63199432 A JP S63199432A
Authority
JP
Japan
Prior art keywords
gas
capillaries
bundled
silicon substrate
dispersing head
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
JP3285387A
Other languages
Japanese (ja)
Other versions
JPH0573257B2 (en
Inventor
Katsuya Okumura
勝弥 奥村
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP3285387A priority Critical patent/JPS63199432A/en
Publication of JPS63199432A publication Critical patent/JPS63199432A/en
Publication of JPH0573257B2 publication Critical patent/JPH0573257B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a device, cost of which is low and which is assembled easily and enables the deposition of doped polysilicon and deposition under decompression of an oxide film when the device is used for a decompression CVD device, by a method wherein a gas path is formed by a plurality of capillaries, the capillaries are bundled while the lower ends of the capillaries are cut to the same plane shape and a gas dispersing head is constituted. CONSTITUTION:A gas path introducing a gas is shaped by a plurality of capillaries 17, and the capillaries 17 are bundled while the lower ends of the capillaries are out to the same plane shape, thus organizing a gas dispersing head 4. A large number of the capillaries 17 made of stainless having an outside diameter of 1mm and an inside diameter of 0.8mm are divided into two of a group of capillaries 17a for silane gas, upper ends of which are employed as gas introducing ports for silane gas and the insides of which are used as paths, and a group of capillaries 17b for oxygen gas, upper ends of which are employed as gas introducing ports for oxygen gas and the insides of which are used as paths, while the capillaries 17 are bundled by a rectangular frame-shaped bundling band 18, the bundled section is formed to approximately 400X100mm, and the lower ends of the capillaries are shaped to a plane shape, thus constructing the gas dispersing head 4.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明はシラン(S iHa )ガスと酸素ガス等から
なる反応ガスを放出させ、この還元と酸化作用によって
シリコン基板の表面及びその近傍にシリコン酸化膜(S
 i02 )を気相成長させて堆積させるCVD (気
相酸化膜被着)装置の、ガスの導入に使用して最適なガ
ス分散ヘッドに関する。
[Detailed Description of the Invention] [Objective of the Invention] (Industrial Application Field) The present invention releases a reactive gas consisting of silane (S iHa ) gas, oxygen gas, etc., and by this reduction and oxidation action, the surface of a silicon substrate is and a silicon oxide film (S
This invention relates to a gas dispersion head that is optimal for use in introducing gas in a CVD (vapor phase oxide deposition) device that deposits i02) by vapor phase growth.

(従来の技術) 従来、常圧下で半導体基板にシリコン酸化膜を堆積させ
る上記CVD装置としては、例えば第5図及び第6図に
示すように、基板支持台1の内部にヒータ2を内蔵し、
この基板支持台1の上面に81したシリコン基板3をこ
のヒータ2で約400℃程度に昇温させ、このシリコン
基板3の垂直り方に位置してガス分散ヘッド4を配置し
たものが一般に知られている。
(Prior Art) Conventionally, the above-mentioned CVD apparatus for depositing a silicon oxide film on a semiconductor substrate under normal pressure has a heater 2 built into a substrate support 1, as shown in FIGS. 5 and 6, for example. ,
It is generally known that a silicon substrate 3 placed on the top surface of the substrate support 1 is heated to about 400° C. by the heater 2, and a gas dispersion head 4 is placed vertically to the silicon substrate 3. It is being

このガス分散ヘッド4は、多数枚の分散板5を積層して
、この内部にガス通路としての上下に連通した複数列の
スリット6を形成し、このスリット6から上記シランガ
スと酸素ガスを分散放出させて、両者の混合ガスである
反応ガス7でシリコン基板3の上面及びその近傍でシリ
コン酸化膜を気相成長させて堆積させるようにしたもの
であった。
This gas dispersion head 4 has a large number of stacked dispersion plates 5, and has a plurality of vertically communicating slits 6 formed therein as gas passages, and the silane gas and oxygen gas are dispersed and released from the slits 6. Then, a silicon oxide film is deposited by vapor phase growth on the upper surface of the silicon substrate 3 and its vicinity using a reactive gas 7 which is a mixture of both gases.

そして、通常このスリット6の幅は1〜2mm5ガス分
散ヘッド4とシリコン基板3との距離は3〜5n++n
で、スリット長さく幅方向直交長さ)は400〜500
mm程度であった。
The width of this slit 6 is usually 1 to 2 mm, and the distance between the gas dispersion head 4 and the silicon substrate 3 is 3 to 5n++n.
The slit length (length perpendicular to the width direction) is 400 to 500.
It was about mm.

この場合、スリット6の長さ方向の膜厚のバラツキは良
好であるが、これと直交する幅方向の膜厚のバラツキが
良くないため、シリコン基板3又はガス分散ヘッド4を
スリット6の幅方向に移動させることにより膜厚の均一
性を向上させていた。
In this case, the film thickness variation in the length direction of the slit 6 is good, but the film thickness variation in the width direction perpendicular to this is not good, so the silicon substrate 3 or the gas dispersion head 4 is The uniformity of the film thickness was improved by moving the film.

また、第7図は従来の減圧CVD装置を示すもので、減
圧可能な石英チューブ製の反応管8の外部には、被膜処
理するシリコン基板3を加熱するためのヒータ9が配置
され、反応管8の一端は排気装置10に接続されている
とともに、他端はシリコン基板3及びこれを保持するた
めの基板ホルダ11の搬入及び搬出を行うための開閉自
在なドア12が備えられ、ここにシール13が介在され
て気密性が確保されている。そして、反応ガスとして使
用されるガス類は、夫々のボンベ14゜15から導入さ
れ、ドア12を通過して反応管8の中で放出される。
Moreover, FIG. 7 shows a conventional low pressure CVD apparatus, in which a heater 9 for heating the silicon substrate 3 to be coated is arranged outside a reaction tube 8 made of a quartz tube that can reduce the pressure. One end of 8 is connected to an exhaust device 10, and the other end is provided with a door 12 that can be opened and closed for loading and unloading the silicon substrate 3 and a substrate holder 11 for holding it. 13 is interposed to ensure airtightness. Gases used as reaction gases are introduced from the respective cylinders 14 and 15, pass through the door 12, and are discharged into the reaction tube 8.

この放出されたガスは、その前方に配置された分散板1
6を通過することにより分散され、シリコン基板3と反
応管8との隙間を通って排気されていく。シリコン基板
3の表面には、この排気流から拡散されて反応ガスの供
給が行われる。
This released gas is transferred to the dispersion plate 1 placed in front of it.
6 and is dispersed, and is exhausted through the gap between the silicon substrate 3 and the reaction tube 8. A reactive gas is supplied to the surface of the silicon substrate 3 by being diffused from this exhaust flow.

このようにして、酸化膜の堆積が行われるため、シリコ
ン基板3と反応管8との隙間やシリコン基板3間の距離
は、減圧CVD装置においては、均一な膜厚を得るため
に重要なものである。
Since the oxide film is deposited in this way, the gap between the silicon substrate 3 and the reaction tube 8 and the distance between the silicon substrates 3 are important in the low pressure CVD apparatus in order to obtain a uniform film thickness. It is.

(発明が解決しようとする問題点) しかしながら、上記第5図及び第6図に示すものは、多
数枚の分散板5を積層して複数列のスリット6を形成し
てガス分散ヘッドを構成しているため、多くの座ぐりや
孔を設ける必要があるばかりでなく、組立て精度も高い
ものが要求され、このため、かなり高価なものとなって
しまっていた。
(Problems to be Solved by the Invention) However, the gas dispersion head shown in FIGS. 5 and 6 above is constructed by stacking a large number of dispersion plates 5 to form a plurality of rows of slits 6. Because of this, it is not only necessary to provide many counterbores and holes, but also requires high assembly precision, making it quite expensive.

史に、9解洗浄するに際しても多大の労力と高度な組立
て技術が必要であった。
Historically, a great deal of labor and sophisticated assembly techniques were required even when disassembling and cleaning.

また、第7図に示すものは、反応管8に導入された反応
ガスは、順次熱分解されながら排気されていくため、導
入口側と排気口側とては、反応ガスの濃度勾配が生じて
膜厚の不均一性か生じてしまう。これを防止するため、
ヒータ9に温度勾配を持たせて膜厚の均一性の向上が図
ることか行われている。
In addition, in the case shown in FIG. 7, the reaction gas introduced into the reaction tube 8 is sequentially thermally decomposed and exhausted, so a concentration gradient of the reaction gas occurs between the inlet port and the exhaust port. This may result in non-uniformity in film thickness. To prevent this,
It has been attempted to improve the uniformity of the film thickness by providing a temperature gradient to the heater 9.

しかしながら、不純物を入れないアンド−ブトポリシリ
コン膜では、この温度勾配を持たせることによって良好
な結果を得ることができるが、リンやヒ素などの不純物
をドープしたドープドポリシリコンの場合には、不純物
の濃度勾配が生じてしまい、膜片の均一性と濃度の均一
性を両立することができなかった。
However, in undoped polysilicon films that do not contain any impurities, good results can be obtained by creating this temperature gradient, but in the case of doped polysilicon films that are doped with impurities such as phosphorous or arsenic, A concentration gradient of impurities occurs, making it impossible to achieve both uniformity of the film pieces and uniformity of concentration.

また、シリコン酸化膜を堆積するため、シラン(S I
H,i )と酸素ガスを導入して膜の堆積を行う場合に
は、シランガスの熱分解が早いため良好な膜厚の均一性
を得ることができないといった問題点があった。
Also, in order to deposit a silicon oxide film, silane (S I
When a film is deposited by introducing H,i) and oxygen gas, there is a problem that good film thickness uniformity cannot be obtained because the silane gas thermally decomposes quickly.

−4一 本発明は上記に鑑み、安価で組立てが容易であるばかり
でなく、減圧CVD装置に使用して、ドープドポリシリ
コンの堆積や酸化膜を減圧下で堆積さぜることかできる
ものを提供することを目的としてなされてものである。
-41 In view of the above, the present invention is not only inexpensive and easy to assemble, but also can be used in a low pressure CVD apparatus to deposit doped polysilicon and oxide films under reduced pressure. It was made with the purpose of providing.

〔発明の構成〕[Structure of the invention]

(問題点を解決するための手段) 本発明は上記目的を達成するため、複数本の細管でガス
を導入するガス通路を形成し、この細管を束ねるととも
に、その下端を同一平面状に切断してガス分散ヘッドを
構成したものであり、平面状の下端を被堆積基板に対面
させ、この被堆積基板にガスが垂直に放出するようにし
てCVD装置に使用するものである。
(Means for Solving the Problems) In order to achieve the above object, the present invention forms a gas passage through which gas is introduced using a plurality of thin tubes, bundles the thin tubes, and cuts the lower ends of the thin tubes into the same plane. The gas dispersion head is used in a CVD apparatus with its flat lower end facing a substrate to be deposited, and gas is discharged perpendicularly to the substrate to be deposited.

(作 用) 而して、内部にガスを導入する複数本の細管を束ねてガ
ス分散ヘッドを構成することにより、この組立てや分解
洗浄等を容易となすとともにコストダウンを図り、更に
下端を被堆積基板に対面させ、この被堆積基板にガスが
垂直に放出するようにして、減圧CVD装置にも使用で
きるようにしたものである。
(Function) By configuring a gas dispersion head by bundling a plurality of thin tubes that introduce gas into the interior, assembly, disassembly and cleaning, etc. can be facilitated, costs can be reduced, and the lower end can be covered. It is made to face the deposition substrate so that gas is discharged vertically to the deposition substrate, so that it can also be used in a low pressure CVD apparatus.

(実施例) 第1図及び第2図は本発明の一実施例を示すもので、外
径1m+nで内径が0.8m+nの多数のステンレス製
の細管17を、上端をシランガスのガス導入口とし内部
を通路とした一群のシランガス用細管17aと、上端を
酸素ガスのガス導入口とし内部を通路とした一群の酸素
ガス用細管17bとに三方するとともに、これを矩形枠
状の束ね帯18で束ね、この束ねた断面がほぼ400X
100mm程度になるようになし、更に下端を平面状に
してガス分散ヘッド4を構成したものである。
(Embodiment) Figures 1 and 2 show an embodiment of the present invention, in which a large number of stainless steel thin tubes 17 with an outer diameter of 1 m+n and an inner diameter of 0.8 m+n are used, with the upper end being a gas inlet for silane gas. A group of thin tubes 17a for silane gas with the inside as a passage and a group of thin tubes 17b for oxygen gas with the upper end as a gas inlet for oxygen gas and the inside as a passage. Bundle, the cross section of this bundle is approximately 400X
The gas dispersion head 4 is made to have a length of about 100 mm, and the lower end is made flat.

このシランガス用細管17aと酸素ガス用細管17bと
は、夫々列を成すよう平行に束ねられている。
The silane gas thin tube 17a and the oxygen gas thin tube 17b are bundled in parallel so as to form rows.

このようしてガス分散ヘッド4を構成することによって
、組立てや分解洗浄等の容易化を図るとともに、通常一
般的に安価な細管17を使用することにより、大幅なコ
ストダウンを図るのである。
By configuring the gas dispersion head 4 in this manner, it is possible to facilitate assembly, disassembly and cleaning, and also to significantly reduce costs by using the generally inexpensive thin tube 17.

第3図は他の実施例を示すもので、シランガス用細管1
7aと酸素ガス用細管17bとが夫々相互に市松模様を
描くように配設するとともに、束ねた断面が披堆積基板
であるシリコン基板とほぼ同じ形状としたものである。
Figure 3 shows another embodiment, in which a capillary tube for silane gas 1
The thin tubes 7a and 17b for oxygen gas are mutually arranged in a checkerboard pattern, and the cross section of the bundle is approximately the same shape as the silicon substrate which is the deposited substrate.

このように配列することによって、面内の均一性を向」
ニさせ、ガス分散ヘッド4とシリコン基板とを対向させ
たまま、移動する必要をなくすようにすることができる
This arrangement improves in-plane uniformity.
This makes it possible to eliminate the need to move the gas dispersion head 4 and the silicon substrate while keeping them facing each other.

第1図に示す実施例では、矩形状の各群のシランガス用
細管17aと酸素ガス用細管17bとを、矩形状に束ね
るでいるが、第4図に示すように、円状の各群のシラン
ガス用細管17aと酸素ガス用細管17bとを、円形枠
状の束ね帯18′で円状に束ねても良い。
In the embodiment shown in FIG. 1, the silane gas thin tubes 17a and the oxygen gas thin tubes 17b of each rectangular group are bundled in a rectangular shape, but as shown in FIG. The silane gas thin tube 17a and the oxygen gas thin tube 17b may be bundled in a circle with a circular frame-shaped binding band 18'.

なお、細管17として円筒状のチューブを使用している
か、これに限ることなく、例えば断面四角形や六角形等
の多角形チューブを用い、チューブ間に隙間か生じない
ようにしても良い。
Note that a cylindrical tube may be used as the thin tube 17, but the present invention is not limited to this; for example, a polygonal tube such as a square or hexagonal cross section may be used to avoid gaps between the tubes.

更に、束ねられた細管17が全てガスの放出用に用いら
れる必要はなく、一部の細管をガス排気に利用するよう
にしても良い。
Furthermore, it is not necessary that all the bundled thin tubes 17 be used for gas discharge, and some of the thin tubes may be used for gas exhaust.

また、細管17の材質としては、経済性から考えるとス
テンレスが望ましいが、耐熱性や耐腐蝕性の観点からは
、石英等のガラスやガラス状カーボン及び他の金属など
を用いることもできる。
Further, as the material for the thin tube 17, stainless steel is desirable from an economic standpoint, but from the standpoint of heat resistance and corrosion resistance, glass such as quartz, glassy carbon, and other metals may also be used.

上記ガス分散ヘッド4を減圧CVD装置に使用した例を
第5図に示す。
FIG. 5 shows an example in which the gas dispersion head 4 is used in a reduced pressure CVD apparatus.

同図のガス分散ヘッド4は外径1 mm、内径0.8n
+mのステンレス製の細管17を、束ねた断面が直径1
.60 mm程度となるようにしたものである。
The gas dispersion head 4 in the figure has an outer diameter of 1 mm and an inner diameter of 0.8 nm.
The cross section of bundled stainless steel tubes 17 of +m has a diameter of 1
.. The length is about 60 mm.

このガス分散ヘッド4を反応管8にシール19を介して
気密性を持たせて取付けたものであり、この反応管8は
排気装置(図示せず)に接続されて、真空にすることが
できるものである。
This gas dispersion head 4 is airtightly attached to a reaction tube 8 via a seal 19, and this reaction tube 8 can be connected to an exhaust device (not shown) to create a vacuum. It is something.

この反応管8の内部には、カーボンで作られた基板支持
台20が、上記ガス分散ヘッド4の下面と対面して配置
され、この基板支持台20の上面には、例えば直径15
0+++n+のシリコン基板3を載置するための凹部が
設けら、この凹部にシリコン基板3を載置した時に、こ
の表面が」1記ガス分散ヘッド4の下面に対面し、ここ
から供給されるガスが、この表面に垂直に放出されるよ
う構成されている。
Inside this reaction tube 8, a substrate support 20 made of carbon is arranged facing the lower surface of the gas dispersion head 4, and on the upper surface of this substrate support 20, there is a
A recess for placing the silicon substrate 3 of 0+++n+ is provided, and when the silicon substrate 3 is placed in this recess, this surface faces the lower surface of the gas dispersion head 4, and the gas supplied from there. is arranged to emit perpendicular to this surface.

この反応管8の外部には、この内部に載置したシリコン
基板3を加熱するための赤外線ランプ2]が配設されて
いる。この赤外線ランプ21の代わりに高周波電源によ
る誘導加熱方式を採用しても良い。
An infrared lamp 2 for heating the silicon substrate 3 placed inside the reaction tube 8 is disposed outside the reaction tube 8. Instead of this infrared lamp 21, an induction heating method using a high frequency power source may be adopted.

そして、この赤外線ランプ21により、シリコン基板3
を450℃に加熱保持し、ガス分散ヘラF’ 4からシ
ランガス及び酸素ガスを放出させるとともに、反応管8
内の圧力を0 、 5 Torrにして、この表面にシ
リコン酸化膜を2%の均一性で堆積させた。
Then, the infrared lamp 21 illuminates the silicon substrate 3.
is heated and maintained at 450°C, silane gas and oxygen gas are released from the gas dispersion spatula F' 4, and the reaction tube 8
The internal pressure was set to 0.5 Torr, and a silicon oxide film was deposited on this surface with a uniformity of 2%.

L記反応管8の左右には、予備室22.23が連接され
、この予備室22.23を用いて反応管8を大気にさら
すことなく、シリコン基板3がロードされ、シリコン酸
化膜の堆積後にアンロードされるよう構成されている。
A preliminary chamber 22.23 is connected to the left and right sides of the L reaction tube 8, and the silicon substrate 3 is loaded using the preliminary chamber 22.23 without exposing the reaction tube 8 to the atmosphere, and a silicon oxide film is deposited. It is configured to be unloaded later.

なお、導入ガスを代えることにより、ドープドポリシリ
コン膜、シリコン窒化膜、タングステン膜、更にはタン
グステンシリサイド膜等を堆積するようにすることがで
きる。
Note that by changing the introduced gas, a doped polysilicon film, a silicon nitride film, a tungsten film, a tungsten silicide film, or the like can be deposited.

この、ドープドポリシリコン膜の堆積は、シリコン基板
3の温度を700℃とし、ガス種としてはシランガスを
、不純物ガスとしてアルシン(A s Ha )を用い
ることにより、ASの膜内の濃度バラツキを1%以下に
抑えることができる。
This doped polysilicon film is deposited by setting the temperature of the silicon substrate 3 to 700°C, using silane gas as the gas type, and arsine (As Ha) as the impurity gas, thereby reducing the concentration variation in the AS film. It can be suppressed to 1% or less.

シリコン窒化膜は、シランガスとアンモニアを用い、シ
リコン基板3の温度を720℃としたり、更には、有機
金属ガスを用いて、この堆積を行うことができる。
The silicon nitride film can be deposited by using silane gas and ammonia at a temperature of 720° C. for the silicon substrate 3, or by using an organic metal gas.

なお、膜厚や膜質の均一性を向上させるために、ガス分
散ヘッド4又はシリコン基板3を移動や回転させても良
く、更には細管17に導入するガスをオン・オフしたり
、ガス種を切換えたりするようにしても良い。
In order to improve the uniformity of the film thickness and film quality, the gas dispersion head 4 or the silicon substrate 3 may be moved or rotated, and the gas introduced into the thin tube 17 may be turned on or off, or the type of gas may be changed. It may also be possible to switch.

〔発明の効果〕〔Effect of the invention〕

本発明は上記のような構成であるので、構造的に簡単で
かつ組立ても容易であるばかりでなく、比較的安価な細
管を使用しているため、大幅なコストダウンを図るとと
もに、分解洗浄の簡便なガス分散ヘッドを提供すること
ができる。
Since the present invention has the above-mentioned configuration, it is not only structurally simple and easy to assemble, but also uses relatively inexpensive thin tubes, which significantly reduces costs and reduces the need for disassembly and cleaning. A simple gas dispersion head can be provided.

更に、減圧CVD装置に使用することにより、ガス濃度
の勾配(むら)を極力小さくすることかでき、大口径等
、大型の被膜基板でも、均質な膜を均−性高く堆積させ
ることができる。
Furthermore, by using it in a low pressure CVD apparatus, the gradient (unevenness) of gas concentration can be minimized, and a homogeneous film can be deposited with high uniformity even on a large coating substrate, such as a large diameter one.

また、ガス放出口からシリコン基板までの距離が小さい
ため、熱分解しやすいガスでもシリコン基板の温度を高
くして堆積することができ、ステップ力バレイジの改善
も図るようにすることもできるといった諸効果がある。
In addition, since the distance from the gas outlet to the silicon substrate is small, even gases that are easily thermally decomposed can be deposited by raising the temperature of the silicon substrate, and it is also possible to improve step force rayage. effective.

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

第1図及び第2図は本発明の一実施例を示し、第1図は
斜視図、第2図は要部を示す横断面図、第3図は他の実
施例を示す第2図相当図、第4図は更に他の実施例を示
す斜視図、第5図は本発明の使用例を示す縦断面図、第
6図及び第7図は従来例を示し、第6図はCVD装置の
縦断面図、第7図はガス分散ヘッドを示す斜視図、第8
図は他の従来例のCVD装置を示す縦断面図である。 3・・・シリコン基板、4・・・ガス分散ヘッド、17
・・・細管、18. 18’・・・束ね帯、20・・・
基板支持台、21・・・赤外線ランプ。 出願人代理人  佐  藤  −雄 =  12 − 1N開日UG3−199432(6) 曽 0 ぐ1 勿O凶
1 and 2 show one embodiment of the present invention, FIG. 1 is a perspective view, FIG. 2 is a cross-sectional view showing main parts, and FIG. 3 is equivalent to FIG. 2 showing another embodiment. 4 is a perspective view showing still another embodiment, FIG. 5 is a vertical sectional view showing an example of use of the present invention, FIGS. 6 and 7 show a conventional example, and FIG. 6 is a CVD apparatus. FIG. 7 is a perspective view showing the gas dispersion head, FIG.
The figure is a longitudinal sectional view showing another conventional CVD apparatus. 3... Silicon substrate, 4... Gas dispersion head, 17
...tubule, 18. 18'... Bundling obi, 20...
Board support stand, 21...infrared lamp. Applicant's agent Sato -O = 12-1N Kaichi UG3-199432 (6)

Claims (1)

【特許請求の範囲】 1、複数本の細管でガスを導入するガス通路を形成し、
この細管を束ねるとともに、その下端を同一平面状に切
断してガス分散ヘッドを構成したことを特徴とするCV
D装置用ガス分散ヘッド。 2、平面状の下端を被堆積基板に対面させ、この被堆積
基板にガスが垂直に放出するようにしたことを特徴とす
る特許請求の範囲第1項記載のCVD装置用ガス分散ヘ
ッド。
[Claims] 1. A gas passage for introducing gas is formed by a plurality of thin tubes,
A CV characterized in that a gas dispersion head is constructed by bundling these thin tubes and cutting their lower ends into the same plane.
Gas dispersion head for D equipment. 2. The gas dispersion head for a CVD apparatus according to claim 1, wherein the planar lower end faces the substrate to be deposited so that gas is emitted perpendicularly to the substrate to be deposited.
JP3285387A 1987-02-16 1987-02-16 Gas dispersing head for cvd device Granted JPS63199432A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3285387A JPS63199432A (en) 1987-02-16 1987-02-16 Gas dispersing head for cvd device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3285387A JPS63199432A (en) 1987-02-16 1987-02-16 Gas dispersing head for cvd device

Publications (2)

Publication Number Publication Date
JPS63199432A true JPS63199432A (en) 1988-08-17
JPH0573257B2 JPH0573257B2 (en) 1993-10-14

Family

ID=12370393

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3285387A Granted JPS63199432A (en) 1987-02-16 1987-02-16 Gas dispersing head for cvd device

Country Status (1)

Country Link
JP (1) JPS63199432A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5284519A (en) * 1990-05-16 1994-02-08 Simon Fraser University Inverted diffuser stagnation point flow reactor for vapor deposition of thin films
EP0955084A1 (en) * 1998-04-27 1999-11-10 Corning Incorporated Redrawn capillary imaging reservoir
US6350618B1 (en) 1998-04-27 2002-02-26 Corning Incorporated Redrawn capillary imaging reservoir
US6468374B1 (en) 1999-02-18 2002-10-22 Corning Incorporated Method of making silica glass honeycomb structure from silica soot extrusion
US6479129B1 (en) 1999-02-18 2002-11-12 Corning Incorporated Titanium-coating silica glass honeycomb structure from silica soot extrusion
US6762061B1 (en) 1998-07-03 2004-07-13 Corning Incorporated Redrawn capillary imaging reservoir
US6884626B1 (en) 1998-04-27 2005-04-26 Corning Incorporated Redrawn capillary imaging reservoir
US6966951B2 (en) * 2001-08-27 2005-11-22 Jusung Engineering Co., Ltd. Apparatus of manufacturing a semiconductor device
DE102008037160A1 (en) * 2008-08-08 2010-02-11 Krones Ag supply device
CN102345513A (en) * 2010-08-03 2012-02-08 通用电气公司 Turbine intercooler

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57104659A (en) * 1980-12-19 1982-06-29 Asahi Glass Co Ltd Discharger for cvd device
JPS59150533A (en) * 1983-02-16 1984-08-28 Nippon Telegr & Teleph Corp <Ntt> Nozzle for synthesizing compound semiconductive membrane

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57104659A (en) * 1980-12-19 1982-06-29 Asahi Glass Co Ltd Discharger for cvd device
JPS59150533A (en) * 1983-02-16 1984-08-28 Nippon Telegr & Teleph Corp <Ntt> Nozzle for synthesizing compound semiconductive membrane

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5284519A (en) * 1990-05-16 1994-02-08 Simon Fraser University Inverted diffuser stagnation point flow reactor for vapor deposition of thin films
EP0955084A1 (en) * 1998-04-27 1999-11-10 Corning Incorporated Redrawn capillary imaging reservoir
US6350618B1 (en) 1998-04-27 2002-02-26 Corning Incorporated Redrawn capillary imaging reservoir
EP1075327A4 (en) * 1998-04-27 2006-01-25 Corning Inc Redrawn capillary imaging reservoir
US6884626B1 (en) 1998-04-27 2005-04-26 Corning Incorporated Redrawn capillary imaging reservoir
US6596237B1 (en) 1998-04-27 2003-07-22 Nicholas F. Borrelli Redrawn capillary imaging reservoir
US6762061B1 (en) 1998-07-03 2004-07-13 Corning Incorporated Redrawn capillary imaging reservoir
US6468374B1 (en) 1999-02-18 2002-10-22 Corning Incorporated Method of making silica glass honeycomb structure from silica soot extrusion
US6548142B1 (en) 1999-02-18 2003-04-15 Corning Incorporated Silica glass honeycomb structure from silica soot extrusion
US6479129B1 (en) 1999-02-18 2002-11-12 Corning Incorporated Titanium-coating silica glass honeycomb structure from silica soot extrusion
US6966951B2 (en) * 2001-08-27 2005-11-22 Jusung Engineering Co., Ltd. Apparatus of manufacturing a semiconductor device
DE102008037160A1 (en) * 2008-08-08 2010-02-11 Krones Ag supply device
US8435350B2 (en) 2008-08-08 2013-05-07 Krones Ag Supply device
CN102345513A (en) * 2010-08-03 2012-02-08 通用电气公司 Turbine intercooler

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