JPS6239532B2 - - Google Patents

Info

Publication number
JPS6239532B2
JPS6239532B2 JP54149726A JP14972679A JPS6239532B2 JP S6239532 B2 JPS6239532 B2 JP S6239532B2 JP 54149726 A JP54149726 A JP 54149726A JP 14972679 A JP14972679 A JP 14972679A JP S6239532 B2 JPS6239532 B2 JP S6239532B2
Authority
JP
Japan
Prior art keywords
film
gas
electrodes
support
uniform
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
Application number
JP54149726A
Other languages
Japanese (ja)
Other versions
JPS5671930A (en
Inventor
Nobuo Kitajima
Kyosuke Ogawa
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.)
Canon Inc
Original Assignee
Canon Inc
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 Canon Inc filed Critical Canon Inc
Priority to JP14972679A priority Critical patent/JPS5671930A/en
Publication of JPS5671930A publication Critical patent/JPS5671930A/en
Publication of JPS6239532B2 publication Critical patent/JPS6239532B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H10SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
    • H10PGENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
    • H10P14/00Formation of materials, e.g. in the shape of layers or pillars
    • H10P14/20Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials
    • H10P14/34Deposited materials, e.g. layers
    • H10P14/3402Deposited materials, e.g. layers characterised by the chemical composition
    • H10P14/3404Deposited materials, e.g. layers characterised by the chemical composition being Group IVA materials
    • H10P14/3411Silicon, silicon germanium or germanium
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical 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
    • C23C16/50Chemical 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 using electric discharges
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical 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
    • C23C16/54Apparatus specially adapted for continuous coating
    • C23C16/545Apparatus specially adapted for continuous coating for coating elongated substrates
    • HELECTRICITY
    • H10SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
    • H10PGENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
    • H10P14/00Formation of materials, e.g. in the shape of layers or pillars
    • H10P14/20Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials
    • H10P14/24Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials using chemical vapour deposition [CVD]

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Plasma & Fusion (AREA)
  • Photoreceptors In Electrophotography (AREA)
  • Photovoltaic Devices (AREA)

Description

【発明の詳細な説明】 本発明は、グロー放電等の放電を利用して、例
えば光導電膜、半導体膜、無機絶縁膜或いは有機
樹脂を形成するに有効な膜形成法に関する。プラ
ズマ現象を利用して、膜形成用の反応ガスを分解
して所定の支持体上に所望の特性を有する膜を形
成しようとする場合、殊に、大面積の膜の場合に
は、全面積に亘つてその膜厚並びに、電気的、光
学的或いは光電的等の物理特性の均一化及び品質
の均一化を計るには、通常の真空蒸着法に較べて
非常に困難が附纒う。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a film forming method that is effective for forming, for example, a photoconductive film, a semiconductor film, an inorganic insulating film, or an organic resin using discharge such as glow discharge. When trying to form a film with desired characteristics on a given support by decomposing a reaction gas for film formation using plasma phenomenon, especially in the case of a large-area film, the total area It is much more difficult to achieve uniform film thickness, uniform physical properties such as electrical, optical, photoelectric, etc., and uniform quality over the course of the process, compared to ordinary vacuum evaporation methods.

例えば、SiH4ガスを放電エネルギーを使つて
分解し支持体上にアモルフアス水素化シリコン
(以後、a−Si:Hと記す)膜を形成して、この
膜の電気物性を利用し様とする場合、この膜の電
気物性が膜形成時の放電強度に大きく依存する
為、膜の全領域における電気物性の均一性を得る
には、膜形成の全領域において放電強度の均一化
を計る必要がある。
For example, when SiH 4 gas is decomposed using discharge energy to form an amorphous silicon hydride (hereinafter referred to as a-Si:H) film on a support, and the electrical properties of this film are to be utilized. Since the electrical properties of this film are highly dependent on the discharge intensity during film formation, in order to obtain uniform electrical properties over the entire film region, it is necessary to equalize the discharge intensity throughout the film formation region. .

この放電強度の均一性は、電界強度、ガス流
量、ガス圧、ガスの導入位置と排出位置の配置、
放電電極の形状、配置等の要素に主に依存する。
The uniformity of this discharge intensity depends on the electric field strength, gas flow rate, gas pressure, arrangement of gas introduction and discharge positions,
It mainly depends on factors such as the shape and arrangement of the discharge electrode.

而乍ら、従来より提案されている膜形成法で
は、上記の諸要素を一義的に決定して、膜形成条
件が最適となる様な均一な放電強度を得ることは
出来ずある程度の条件緩和の下で膜形成を行なつ
ているのが現状である。
However, with the film formation methods that have been proposed so far, it is not possible to uniquely determine the above factors and obtain a uniform discharge intensity that optimizes the film formation conditions. At present, film formation is performed under the following conditions.

又、大面積の膜を生産性、及び量産性良く形成
するには、ガスの消費が出来るだけ膜形成用だけ
になる様にガス消費量を経済化する事、反応ガス
濃度が膜形成領域で不均一分布しない様にするこ
と、多量のキヤリアガスを要しない様にする事、
膜成長速度の向上を計る事、等々が拳げられ、更
に均一特性と良好な品質の大面積の膜を得るに
は、成長膜厚分布が均一である事、放電によつて
生ずるガスプラズマに空間的不均一分布が生じな
い様にする事等が必要である。従来法は、これ等
の諸点に於いても充分満足し得るものではなく、
生産技術上必要な性能を有する装置の具現化を計
る事が出来なかつた。
In addition, in order to form a large-area film with good productivity and mass production, it is necessary to economize gas consumption so that as much gas as possible is consumed only for film formation, and to reduce the concentration of the reaction gas in the film formation area. To avoid uneven distribution, and to avoid requiring a large amount of carrier gas.
In order to obtain a large-area film with uniform characteristics and good quality, efforts are being made to improve the film growth rate, and to obtain a large-area film with uniform characteristics and good quality, it is necessary to ensure that the grown film thickness distribution is uniform and that the gas plasma generated by the discharge It is necessary to prevent spatial non-uniform distribution from occurring. Conventional methods are not fully satisfactory in these respects,
It was not possible to realize a device with the necessary performance in terms of production technology.

本発明は、上記の諸点に鑑み成されたものであ
つて、大きな面積の膜であつても全面積に亘つ
て、その物理的特性及び膜厚が実質的に均一であ
る膜が再現性良く高効率で形成され得る膜形成法
を提供するのを主たる目的とする。
The present invention has been made in view of the above points, and is capable of producing a film with substantially uniform physical properties and film thickness over the entire area even if the film has a large area with good reproducibility. The main objective is to provide a method for forming a film that can be formed with high efficiency.

又、本発明は、マスプロダクトに極めて有効な
膜形成法を提供することをも目的とする。
Another object of the present invention is to provide a method of forming a film that is extremely effective for mass products.

又、別には本発明は、放電強度が全膜形成領域
に亘つて均一にする事が出来、ガス消費量を極力
低減し得、且つ膜成長速度の大きい、極めて経済
的で生産性に富む膜形成法を提供することも目的
の1つである。
In addition, the present invention provides an extremely economical and highly productive film in which the discharge intensity can be made uniform over the entire film formation area, gas consumption can be reduced as much as possible, and the film growth rate is high. It is also an objective to provide a method of formation.

本発明の膜形成法は減圧にし得る堆積室内に膜
形成用のガスを導入し、放電を利用して所定の支
持体上に膜を形成する膜形成法に於いて、前記堆
積室内に放電を起させるに際して、互いに略々平
行に且つ前記支持体に略々垂直に一列に配した
2n枚の板状電極の(2k−1)番目と2k番目(k
=1,2,3,…n)とで一対にした電極間に電
位差を形成すること、該電位差の形成される電極
間領域に膜形成用のガスの流れを形成することを
特徴とするものである。
The film forming method of the present invention involves introducing a film forming gas into a deposition chamber that can be made under reduced pressure, and forming a film on a predetermined support using electrical discharge. When raised, they are arranged in a line substantially parallel to each other and substantially perpendicular to the support.
(2k−1)th and 2kth (k
= 1, 2, 3,...n), forming a potential difference between a pair of electrodes, and forming a flow of gas for film formation in the region between the electrodes where the potential difference is formed. It is.

この様な本発明の膜形成法によれば全面積に亘
つて、この膜厚並びに電気的、光学的或いは光電
的特性等の物理特性の均一化及び膜品質の均一化
を、大面積に亘つて行なう事が出来、大面積を要
する例えば、太陽電池、電子写真用感光体、或い
は大型テレビ、大型デイスプレイ等の光電変換層
の形成に極めて有効である。
According to the film forming method of the present invention, the film thickness and physical properties such as electrical, optical, or photoelectric properties can be made uniform over the entire area, and the film quality can be made uniform over a large area. It is extremely effective for forming photoelectric conversion layers for solar cells, electrophotographic photoreceptors, large-sized televisions, large-sized displays, etc., which require a large area.

又、更には、ガス消費量が少なく、且つ膜成長
速度が大きいので極めて経済的で生産性に富み、
企業ベースにのり得るものである。
Moreover, it is extremely economical and highly productive because it consumes less gas and has a higher film growth rate.
This can be applied on a corporate basis.

以下、本発明の膜形成法を図面に従つて説明す
る。
The film forming method of the present invention will be explained below with reference to the drawings.

第1図は、本発明の膜形成法を具現化し得る装
置の好適な例の1つの概要を模式的に示した説明
図であり、第2図は第1図の装置の一部を詳細に
説明する為の模式的部分斜視図である。
FIG. 1 is an explanatory diagram schematically showing an outline of a preferred example of an apparatus that can embody the film forming method of the present invention, and FIG. 2 shows a part of the apparatus shown in FIG. 1 in detail. FIG. 2 is a schematic partial perspective view for explanation.

第1図に示される装置100の減圧にし得る堆
積室101の内部には、供給ローラ102に所定
長さ分、巻回された膜形成用の支持体103が案
内支持板104上を誘導されて、その先端が巻取
ローラ105に取付けられて図示の様に膜形成の
準備が成される。
Inside the deposition chamber 101 of the apparatus 100 shown in FIG. , its tip is attached to the take-up roller 105 and preparations for film formation are made as shown in the figure.

案内支持板104の下方には、膜形成用の支持
体103を膜形成中、所定の温度に加熱する為の
ヒータ106が設置されてあつて必要に応じて支
持体103を加熱し得る様になつている。支持体
103の上側には、多数枚(図に於いては16枚)
の板状電極107が互いには略々平行になり、且
つ支持体103には略々垂直になる様に所定の間
隔を置いて横一列に配列されている。
A heater 106 is installed below the guide support plate 104 to heat the support 103 for film formation to a predetermined temperature during film formation, so that the support 103 can be heated as necessary. It's summery. There are many sheets (16 sheets in the figure) on the upper side of the support body 103.
The plate-shaped electrodes 107 are arranged in a horizontal line at predetermined intervals so as to be substantially parallel to each other and substantially perpendicular to the support 103.

図に於いて、16枚の板状電極107は、隣り同
志一対で一組とされて、六組の放電電極が構成さ
れ、各組の放電電極は電気的に絶縁されて上部で
接続され、ガス導入パイプ108で支持されてお
り、堆積室101へのガスの導入は、このガス導
入パイプ108を通じて各組を構成する板状電極
107の間より成される。
In the figure, 16 plate-shaped electrodes 107 are arranged in pairs with adjacent ones to form six sets of discharge electrodes, and each set of discharge electrodes is electrically insulated and connected at the upper part. It is supported by a gas introduction pipe 108, and gas is introduced into the deposition chamber 101 through this gas introduction pipe 108 between the plate electrodes 107 constituting each set.

16枚の板状電極107は、1つ置きに電気的に
共通に接続され、電源109を動作状態にするこ
とによつて各組の電極間に於いて電位差が形成さ
れる。
The 16 plate-like electrodes 107 are electrically connected every other pair in common, and by activating the power source 109, a potential difference is created between each set of electrodes.

電位差の形成された各組の電極間にガス導入パ
イプ108より膜形成用のガスを導入して、ガス
の流れを形成すると該ガスの流れる領域に於いて
放電が引起されて該ガスのプラズマが形成され
る。
When a film-forming gas is introduced from the gas introduction pipe 108 between each set of electrodes having a potential difference to form a gas flow, a discharge is caused in the region where the gas flows, and plasma of the gas is generated. It is formed.

支持体103は、膜形成時に於いて、巻取ロー
ラ105の巻取動作に従つて、その表面が移動さ
れ乍らその表面上に膜形成物質を堆積する。従つ
て、図示する如くの電極配列とガスの導入法によ
つて支持体103の移動方向に垂直な方向への膜
形成条件の均一化が計れ、支持体103の移動し
乍らの膜形成物質の堆積によつて移動方向の膜形
成条件の平均化が計れるので、結果的には、支持
体103上に形成される膜の作成条件が2次元的
に均一化が計れ、大面積に亘つて均一層厚、均一
特性の膜を支持体103上に形成する事が出来
る。
During film formation, the surface of the support 103 is moved according to the winding operation of the winding roller 105, and a film-forming substance is deposited on the surface thereof. Therefore, by using the electrode arrangement and gas introduction method as shown in the figure, it is possible to equalize the film forming conditions in the direction perpendicular to the moving direction of the support 103, and the film forming substance is As a result, the film forming conditions in the moving direction can be equalized by the deposition of A film with uniform layer thickness and uniform properties can be formed on the support 103.

支持体103の膜形成時に於ける移動スピード
は形成される膜に要求される特性、ガス流量、ガ
スの種類、電極107間に形成される電位差の大
きさ、支持体103の種類、堆積スピード
(deposition rate)等に依存し、これ等の条件に
従つて所望により決められるものである。堆積室
101へ導入されるガスは、ガス導入パイプ10
8に接続されてあるボンベ110−1,110−
2,110−3の各々より各々のバルブ111−
1,111−2,111−3を開放することで供
給される。
The moving speed of the support 103 during film formation depends on the characteristics required for the film to be formed, the gas flow rate, the type of gas, the magnitude of the potential difference formed between the electrodes 107, the type of support 103, and the deposition speed ( deposition rate), etc., and can be determined as desired according to these conditions. Gas introduced into the deposition chamber 101 is supplied through a gas introduction pipe 10.
cylinders 110-1, 110- connected to
2,110-3 to each valve 111-
It is supplied by opening 1,111-2,111-3.

例えばa−Si:H膜を形成するのであれば、ボ
ンベ110−1にはSiH4等のシランが、ボンベ
110−2には、不純物導入用のガス、pH3
B2H6等が、又ボンベ110−3には稀釈ガスと
してAr,He等が充填され、これ等のガスは、バ
ルブ111−1,111−2,111−3の開放
度合を調整することで所望の混合比で堆積室10
1内に導入される。
For example, if an a-Si:H film is to be formed, the cylinder 110-1 contains silane such as SiH 4 and the cylinder 110-2 contains gas for introducing impurities, pH 3 ,
B 2 H 6 , etc., and the cylinder 110-3 is filled with Ar, He, etc. as a diluting gas, and these gases are adjusted by adjusting the degree of opening of the valves 111-1, 111-2, and 111-3. in the deposition chamber 10 at the desired mixing ratio.
1.

堆積室101内を減圧にするには、堆積室10
1の下部位に設けられてある排気口112を通じ
て、メインバルブ113を開放することで排気装
置114によつて内部を排気することによつて成
される。
To reduce the pressure inside the deposition chamber 101,
This is accomplished by opening the main valve 113 through an exhaust port 112 provided at the lower portion of the exhaust system 114 to exhaust the inside.

排気装置114は、通常使用されているものが
採用され、例えば堆積室101を低真空程度にす
るのであれば、ロータリーポンプ等だけで良く、
更に高真空にする必要があるならば、拡散ポンプ
等を採用する。
As the exhaust device 114, a commonly used device is adopted; for example, if the deposition chamber 101 is to be brought to a low vacuum level, a rotary pump or the like may be sufficient.
If it is necessary to create an even higher vacuum, use a diffusion pump or the like.

第1図に示される電極配列構造の装置に於いて
は、図に矢印で示してある様に、ガス導入パイプ
108の各流出口より流出されるガスの流れが形
成される。
In the device having the electrode arrangement structure shown in FIG. 1, a flow of gas is formed to flow out from each outlet of the gas introduction pipe 108, as indicated by the arrows in the figure.

この様なガスの流れの形成は、電極配列構造と
の相乗効果によつて、形成されるプラズマ密度の
均一化に大いに効用がある。
Formation of such a gas flow has a synergistic effect with the electrode arrangement structure, and is highly effective in making the density of the formed plasma uniform.

又、形成されるプラズマ雰囲気を、図示の如く
の電極配列構造と、電界の形成を多数の板状電極
の採用によつて空間的に細分化して行う事で電極
の形状や大きさ及び材質的バラツキによる電界の
不均一を平均化して実質上均一化を計ることが出
来、膜の再現性及び特性を飛躍的に向上させるこ
とが出来る。
In addition, the plasma atmosphere that is formed is spatially subdivided by using the electrode arrangement structure shown in the figure and the formation of the electric field by employing a large number of plate-shaped electrodes, so that the shape, size, and material of the electrodes can be controlled. The non-uniformity of the electric field due to variations can be averaged out to make it substantially uniform, and the reproducibility and characteristics of the film can be dramatically improved.

又、図に示す如き、電極配列構造は、装置の大
きさに殆んど関係なく、空間的にバラツキの殆ん
どないプラズマ雰囲気を形成することが出来る。
従つて生産量を上げる意味で生産計画に従つて装
置の大型化を計つても大型化に伴う設計的変更は
殆んどしなくても済むものである。
Further, the electrode array structure as shown in the figure can form a plasma atmosphere with almost no spatial variation, almost regardless of the size of the device.
Therefore, even if the size of the device is increased according to the production plan in order to increase the production volume, there is almost no need to make any design changes due to the increase in size.

更に第1図に示す如き電極配列構造とガス導入
法を採用すると、導入されるガスが膜形成に有効
に消費されるので、未使用のまま堆積室101外
に排出されるガス量は、極めて低く、従つてガス
の消費量を著しく低下させることが出来る。
Furthermore, if the electrode arrangement structure and gas introduction method shown in FIG. 1 are adopted, the introduced gas is effectively consumed for film formation, so the amount of unused gas discharged outside the deposition chamber 101 is extremely reduced. gas consumption can therefore be significantly reduced.

第2図には、第1図に示される装置の電極配列
構造とその形状を詳細に示す為の部分斜視図であ
る。
FIG. 2 is a partial perspective view showing in detail the electrode array structure and shape of the device shown in FIG. 1.

一組の電極、例えば電極107−1と電極10
7−2とか一対とされ、上方が屋根型になつて互
いに電気的に絶縁されて、ガス導入パイプ108
の分析パイプ108−1と一体的構造とされてい
る。
a set of electrodes, e.g. electrode 107-1 and electrode 10
7-2, the upper part is roof-shaped and electrically insulated from each other, and the gas introduction pipe 108
It has an integral structure with the analysis pipe 108-1.

分析パイプ108−1の先端は、T字型とさ
れ、支持体103に向つた側に多数の細孔が、開
けられており、電極107−1,107−2との
間にガスの流れを形成し得る。
The tip of the analysis pipe 108-1 is T-shaped and has many pores opened on the side facing the support 103 to allow gas flow between it and the electrodes 107-1 and 107-2. can be formed.

電極107と支持体103との間に設けられる
間隔は、通常0.5〜6mmとされ、好ましくは1〜
5mmとされる。
The distance provided between the electrode 107 and the support 103 is usually 0.5 to 6 mm, preferably 1 to 6 mm.
It is said to be 5mm.

又、板状電極の配列間隔は、他の膜形成条件と
の相関関係に基いて適宜決められるものであるが
通常2〜5cmとされるのが望ましいものである。
Further, the arrangement interval of the plate electrodes can be appropriately determined based on the correlation with other film forming conditions, but it is usually desirable to set it to 2 to 5 cm.

一対の板状電極間に形成される電位差は、直流
によつてでも交流によつてでも良いものであるが
本発明の場合にはRF(radio freguency)領域の
交流が好ましく採用される。
The potential difference formed between the pair of plate-like electrodes may be caused by direct current or alternating current, but in the case of the present invention, alternating current in the RF (radio frequency) region is preferably employed.

第1図に示す装置によつて実際に膜形成した場
合の1例を示せば、例えば板状電極間を3cmに保
持し、堆積室101の内圧を0.1Torr、反応ガス
流量を0.1c.c./sec、反応ガスとしてSiH4/Ar=
1/10、板状電極の先端と支持体との間隔とを2mm
として、13.56MHz、50Wの電気エネルギーを板
状電極に投入した場合、膜成長度は10Å/secで
電気的、光学的に極めて良好な特性を示すa−
Si:H膜が大面積に亘つて再現性良く形成するこ
とが出来た。
An example of a case where a film is actually formed using the apparatus shown in FIG. 1 is that, for example, the distance between the plate electrodes is maintained at 3 cm, the internal pressure of the deposition chamber 101 is 0.1 Torr, and the reaction gas flow rate is 0.1 cc/sec. , SiH 4 /Ar= as reaction gas
1/10, the distance between the tip of the plate electrode and the support is 2 mm
When electrical energy of 13.56MHz and 50W is applied to the plate electrode, the film growth rate is 10 Å/sec, which shows extremely good electrical and optical properties.
A Si:H film could be formed over a large area with good reproducibility.

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

第1図は、本発明の膜形成法を具現化する為の
装置の1つを示す模式的説明図、第2図は、第1
図の装置を部分的に詳細に示す部分斜視図であ
る。 100……堆積装置、101……堆積室、10
2……供給ローラ、103……支持体、104…
…案内支持板、105……巻取ローラ、106…
…ヒータ、107……板状電極、108……ガス
導入パイプ、109……電源、110……ボン
ベ、111……バルブ、112……排出口、11
3……メインバルブ、114……排気装置。
FIG. 1 is a schematic explanatory diagram showing one of the apparatuses for embodying the film forming method of the present invention, and FIG.
1 is a partial perspective view showing some details of the illustrated device; FIG. 100... Deposition device, 101... Deposition chamber, 10
2... Supply roller, 103... Support body, 104...
...Guide support plate, 105... Winding roller, 106...
... Heater, 107 ... Plate electrode, 108 ... Gas introduction pipe, 109 ... Power supply, 110 ... Cylinder, 111 ... Valve, 112 ... Discharge port, 11
3...Main valve, 114...Exhaust device.

Claims (1)

【特許請求の範囲】 1 減圧にし得る堆積室内に膜形成用のガスを導
入し、放電を利用して所定の支持体上に膜を形成
する膜形成法に於いて、前記堆積室内に放電を起
させるに際して、 互いに略々平行に且つ前記支持体に略々垂直に一
列に配した2n枚の板状電極の(2k−1)番目と
2k番号(k=1,2,3…n)とで一対にした
電極間に電位差を形成すること、該電位差の形成
される電極間領域に膜形成用のガスの流れを形成
すること、 を特徴とする膜形成法。
[Scope of Claims] 1. In a film forming method in which a film forming gas is introduced into a deposition chamber that can be reduced in pressure and a film is formed on a predetermined support using electric discharge, an electric discharge is introduced into the deposition chamber. When raising, the (2k-1)th and
2k numbers (k = 1, 2, 3...n) to form a potential difference between a pair of electrodes, and to form a flow of gas for film formation in the region between the electrodes where the potential difference is formed. Characteristic film formation method.
JP14972679A 1979-11-19 1979-11-19 Film formation Granted JPS5671930A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14972679A JPS5671930A (en) 1979-11-19 1979-11-19 Film formation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14972679A JPS5671930A (en) 1979-11-19 1979-11-19 Film formation

Publications (2)

Publication Number Publication Date
JPS5671930A JPS5671930A (en) 1981-06-15
JPS6239532B2 true JPS6239532B2 (en) 1987-08-24

Family

ID=15481461

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14972679A Granted JPS5671930A (en) 1979-11-19 1979-11-19 Film formation

Country Status (1)

Country Link
JP (1) JPS5671930A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0382403A (en) * 1989-08-28 1991-04-08 Matsushita Electric Works Ltd Elevating/sinking table

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56150874A (en) * 1980-04-23 1981-11-21 Teijin Ltd Method of continuously manufacturing amorphous silicon solar battery
JPS6059729A (en) * 1983-09-12 1985-04-06 Sanyo Electric Co Ltd Preparation of semiconductor film
JPS6059728A (en) * 1983-09-12 1985-04-06 Sanyo Electric Co Ltd Preparation of semiconductor film
FR2550007A1 (en) * 1983-07-29 1985-02-01 Sanyo Electric Co Method for producing a semiconducting film and photovoltaic device obtained by the method
JPH0763057B2 (en) * 1984-11-12 1995-07-05 鐘淵化学工業株式会社 Multi-electrode thin film forming method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0382403A (en) * 1989-08-28 1991-04-08 Matsushita Electric Works Ltd Elevating/sinking table

Also Published As

Publication number Publication date
JPS5671930A (en) 1981-06-15

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