JPH0522376B2 - - Google Patents

Info

Publication number
JPH0522376B2
JPH0522376B2 JP63292203A JP29220388A JPH0522376B2 JP H0522376 B2 JPH0522376 B2 JP H0522376B2 JP 63292203 A JP63292203 A JP 63292203A JP 29220388 A JP29220388 A JP 29220388A JP H0522376 B2 JPH0522376 B2 JP H0522376B2
Authority
JP
Japan
Prior art keywords
substrate
reactive gas
pair
electrodes
plasma
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
JP63292203A
Other languages
Japanese (ja)
Other versions
JPH01157520A (en
Inventor
Shunpei Yamazaki
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.)
Semiconductor Energy Laboratory Co Ltd
Original Assignee
Semiconductor Energy Laboratory 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 Semiconductor Energy Laboratory Co Ltd filed Critical Semiconductor Energy Laboratory Co Ltd
Priority to JP63292203A priority Critical patent/JPH01157520A/en
Publication of JPH01157520A publication Critical patent/JPH01157520A/en
Publication of JPH0522376B2 publication Critical patent/JPH0522376B2/ja
Granted legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/50Photovoltaic [PV] energy

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  • Photovoltaic Devices (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、被膜特に半導体被膜等を成膜するの
に用いられるプラズマ気相反応装置およびプラズ
マ気相反応方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a plasma vapor phase reaction apparatus and a plasma vapor phase reaction method used for forming films, particularly semiconductor films, etc.

〔従来の技術〕[Conventional technology]

従来より知られたプラズマ気相反応装置の構造
として、平行平板型の電極の一方の電極面に平行
に基板を配置するものが知られている。
As a conventionally known structure of a plasma vapor phase reactor, one in which a substrate is arranged parallel to one electrode surface of a parallel plate type electrode is known.

この場合電極間において印加される電界(一般
に高周波電界が用いられる)は、基板に対し垂直
になる。
In this case, the electric field (generally a high frequency electric field is used) applied between the electrodes is perpendicular to the substrate.

また反応性気体の導入方法も電極の他方より被
形成面に垂直方向に反応性気体がふき出す方式
や、反応容器内に単に反応性気体のガスを導入
し、反応容器全体に反応性気体を充満させ、特に
反応性気体に一方方向へのガス流を構成させるこ
となく供給する方式等が知られている。
In addition, there are two methods for introducing reactive gas: a method in which the reactive gas is blown out from the other side of the electrode in a direction perpendicular to the surface to be formed, and a method in which the reactive gas is simply introduced into the reaction vessel, filling the entire reaction vessel with the reactive gas. Methods are known in which the reactor is filled with gas, and in particular, a reactive gas is supplied without forming a gas flow in one direction.

〔従来技術の問題点〕[Problems with conventional technology]

上記従来より知られている平行平板型のプラズ
マ気相反応方法においては、被膜の成長速度が
0.1〜2Å/秒と小さいという問題がある。
In the conventionally known parallel plate type plasma vapor phase reaction method mentioned above, the growth rate of the film is
There is a problem in that it is small at 0.1 to 2 Å/sec.

特に反応性気体を反応容器内全体に充満させる
方式においては、0.1〜0.4Å/秒と極めて小さ
く、加えて反応生成物がフレーク状にチヤンバー
内壁に付着し、それらが基板上に落下してピンホ
ールの発生を誘発してしまうという問題があつ
た。
In particular, in the method of filling the entire reaction chamber with reactive gas, the reaction product is extremely small at 0.1 to 0.4 Å/sec, and in addition, reaction products adhere to the inner wall of the chamber in the form of flakes, which fall onto the substrate and become pinned. There was a problem in that it induced the formation of holes.

また上記平行平板型の装置においては、基板が
一方の電極上に電極と平行に配置されるので、そ
の生産性が低いという問題があつた。例えば太陽
電池を作製した場合、その製造原価は10cm2の基板
の大きさにて5000円をこえ、さらにその内の4000
円以上は設備償却費という全く非常識な現状であ
つた。
Further, in the above-mentioned parallel plate type device, since the substrate is arranged on one electrode in parallel with the electrode, there is a problem that the productivity is low. For example, when producing a solar cell, the manufacturing cost exceeds 5,000 yen for a 10 cm 2 substrate, and 4,000 yen of that amount
The current state of affairs was completely absurd, with costs exceeding 100,000 yen being depreciation costs for equipment.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明は、上記従来の平行平板型のプラズマ気
相反応装置の問題点である、「反応性気体の利用
効率の悪さ(成膜効率の悪さ)」、「同時に成膜で
きる基板数の少なさ」といつた問題を解決し、生
産性の高いプラズマ気相反応装置、およびこの装
置を用いたプラズマ気相反応方法を得ることを目
的とする。
The present invention addresses the problems of the conventional parallel plate type plasma gas phase reactor described above, such as "inefficient use of reactive gas (poor film forming efficiency)" and "small number of substrates that can be simultaneously formed. The purpose of this study is to solve the above problems and to obtain a highly productive plasma vapor phase reaction device and a plasma vapor phase reaction method using this device.

〔課題を解決するための手段〕[Means to solve the problem]

(第1の発明) 本発明の第1は、反応性気体を導入する手段及
び排出する手段と、一対の電極と、一対のガイド
と、前記一対の電極間に複数の基板を被形成面を
離間して保持する手段と、前記複数の基板全体を
囲む構造の移動可能な基板支持体と、有したプラ
ズマ気相反応装置であつて前記一対のガイドと前
記基板支持体とにより、前記複数の基板は閉空間
に閉じ込められ、反応性気体が前記基板の被形成
面に対し概略平行に流れるように、前記反応性気
体を導入する手段及び排出する手段とが設けら
れ、前記一対の電極から印加されるプラズマを生
じせしめる電界が前記基板の被形成面に対し概略
平行に加えられるように、前記一対の電極は設け
られ、前記反応性気体の流れと前記プラズマを生
じせしめる電界とが互いに概略直交するように、
前記反応性気体を導入する手段及び排出する手段
と前記一対の電極とが設けられている、という構
成を要旨とするものである。
(First Invention) The first aspect of the present invention is to provide a means for introducing and discharging a reactive gas, a pair of electrodes, a pair of guides, and a plurality of substrates between the pair of electrodes. a means for holding the plurality of substrates apart; a movable substrate support having a structure surrounding the entirety of the plurality of substrates; The substrate is confined in a closed space, and means for introducing and discharging the reactive gas are provided so that the reactive gas flows approximately parallel to the surface on which the substrate is formed, and the reactive gas is applied from the pair of electrodes. The pair of electrodes are provided such that the electric field that generates the plasma is applied approximately parallel to the formation surface of the substrate, and the flow of the reactive gas and the electric field that generates the plasma are approximately orthogonal to each other. As you do,
The gist of the configuration is that means for introducing and discharging the reactive gas, and the pair of electrodes are provided.

(第2の発明) 本発明の第2は、反応性気体を導入する手段及
び排出する手段と、一対の電極と、一対のガイド
と、前記一対の電極間に複数の基板を被形成面を
離間して保持する手段と、前記複数の基板全体を
かこむ構造の移動可能な基板支持体と、有したプ
ラズマ気相反応装置を用いたプラズマ気相反応方
法であつて、基板は前記一対のガイドと前記基板
支持体とにより、閉空間に閉じ込められており、
反応性気体は前記基板の被形成面に対し概略平行
に流され、前記一対の電極から印加されるプラズ
マを生じせしめる電界は前記基板の被形成面に対
して概略平行に加えられ、かつ前記反応性気体の
流れと前記プラズマを生じせしめる電界とが互い
に概略直交するようにしてプラズマ気相反応を行
う、という構成を要旨とするものである。
(Second Invention) The second aspect of the present invention is to provide a means for introducing and discharging a reactive gas, a pair of electrodes, a pair of guides, and a plurality of substrates between the pair of electrodes. A plasma vapor phase reaction method using a plasma vapor phase reaction apparatus comprising: a means for holding the plurality of substrates apart; and the substrate support, and are confined in a closed space,
The reactive gas is flowed approximately parallel to the formation surface of the substrate, the electric field for generating plasma applied from the pair of electrodes is applied approximately parallel to the formation surface of the substrate, and the reaction gas is flowed approximately parallel to the formation surface of the substrate. The gist of this is that the plasma gas phase reaction is carried out in such a way that the flow of the gas and the electric field that generates the plasma are approximately perpendicular to each other.

本発明において、複数の基板を該基板をかこむ
構造の基板支持体でもつて保持し、成膜の際、該
基板支持体と一対のガイドによつて、閉空間を形
成し該閉空間内に基板を保持することによつて、
高い成膜性を得るものである。
In the present invention, a plurality of substrates are held by a substrate support having a structure surrounding the substrates, and during film formation, a closed space is formed by the substrate support and a pair of guides, and the substrates are held in the closed space. By holding the
This provides high film formability.

また基板の被形成面に概略平行に反応性気体を
流し、印加電界も基板の被形成面に概略平行にす
ることにより、反応性気体の利用効率を高めるこ
とができる。
Further, by flowing the reactive gas approximately parallel to the surface on which the substrate is formed and applying an electric field approximately parallel to the surface on which the substrate is to be formed, it is possible to increase the utilization efficiency of the reactive gas.

さらに一対の電極から印加電界によつて発生す
るプラズマが基板支持体と一対のガイドによつて
形成される閉空間に閉じ込められることになるの
で、プラズマが反応容器内部全体に広がらず ・効率良く成膜ができる。
Furthermore, since the plasma generated by the electric field applied from the pair of electrodes is confined in the closed space formed by the substrate support and the pair of guides, the plasma does not spread throughout the interior of the reaction vessel and is efficiently generated. A film is formed.

・反応容器内壁を汚染しない。・Do not contaminate the inner wall of the reaction vessel.

という効果を得ることができる。This effect can be obtained.

以下に本発明を利用した実施例を示し、本発明
を具体的な例に則して説明する。
Examples utilizing the present invention will be shown below, and the present invention will be explained based on specific examples.

〔実施例〕〔Example〕

本実施例の構成を第4図に示す。 The configuration of this embodiment is shown in FIG.

図面において反応性気体は気体導入系26,2
7,28より導入口66をへて導出口18より横
方向に噴き出される。また反応後の不用気体は排
出口21をへて76よりロータリーポンプ37に
排気される。基板2は鉛直方向に立てて林立さ
せ、基板支持体(ホルダ)74により空間に保持
されている。反応性気体はガイド70,71によ
り横型の筒状空間に選択的に流れるようになつて
いる。
In the drawing, the reactive gas is the gas introduction system 26, 2.
7, 28, passes through the inlet 66, and is ejected laterally from the outlet 18. Further, the unnecessary gas after the reaction is exhausted from the exhaust port 21 to the rotary pump 37 via 76. The substrates 2 are arranged vertically in a row and are held in space by a substrate support (holder) 74. Guides 70 and 71 allow the reactive gas to flow selectively into the horizontal cylindrical space.

プラズマを生じせしめる電界は、高周波電源1
5より一対の電極67,72を通して、鉛直に保
持された複数の電極の被形成面に平行に印加され
る。ここで基板支持体74と一対のガイド70,
71によつて閉空間が形成され発生したプラズマ
が閉じ込められるので、反応効率を高めることが
でき、しかも反応容器内壁に不用な成膜を行うこ
とがない構成をとることができる。
The electric field that generates plasma is generated by a high frequency power source 1.
The voltage is applied in parallel to the formation surfaces of the plurality of vertically held electrodes through a pair of electrodes 67 and 72 from 5. Here, a substrate support 74 and a pair of guides 70,
Since a closed space is formed by 71 and the generated plasma is confined, the reaction efficiency can be increased and a configuration can be adopted in which unnecessary film formation is not performed on the inner wall of the reaction vessel.

さらに本実施例においては第4図にその基本構
造を示すように、一対の電極67,72の間で加
えられる電界の向きと(第4図でいう上下方向)、
反応性気体の導入口66より導入され排出口21
に排出される反応性気体の流れの向き(第4図で
いう右から左への方向)とが概略直交する構造と
なつている。
Furthermore, in this embodiment, as the basic structure is shown in FIG. 4, the direction of the electric field applied between the pair of electrodes 67 and 72 (vertical direction in FIG. 4),
The reactive gas is introduced from the inlet 66 and discharged from the outlet 21.
The structure is such that the direction of the flow of the reactive gas discharged into the reactor (the direction from right to left in FIG. 4) is approximately perpendicular to the flow direction.

また基板加熱用に、赤外線ランプは12,1
2′を上下に設け、均一な加熱ができるように構
成させている。
In addition, an infrared lamp is used for heating the substrate.
2' are provided above and below to ensure uniform heating.

本実施例のような構成をとつた場合、基板2支
持体74の系〜への移動が容易であるという
特性を有し、多量生産を行うのに優れた構造であ
る。
When the configuration of this embodiment is adopted, the substrate 2 support 74 can be easily moved from one system to another, and is an excellent structure for mass production.

本実施例において成膜される被膜としては、水
素またはハロゲン元素が添加された非単結晶半導
体層をその代表例として挙げることができる。
A typical example of the film formed in this example is a non-single crystal semiconductor layer to which hydrogen or a halogen element is added.

具体的には、珪素、ゲルマニユーム、炭化珪素
(SiCのみではなく、本発明においてはSixC1-x
<X<1の総称を意味する)、珪化ゲルマニユー
ム(SixGe1-x0<X<1)、珪化スズ(SixSn1-x
0<X<1)を挙げることができる。
Specifically, silicon, germanium, silicon carbide (not only SiC, but also SixC 1-x 0 in the present invention)
<X<1), germanium silicide (SixGe 1-x 0<X<1), tin silicide (SixSn 1-x
0<X<1).

また反応容器を複数連結することにより、Pま
たはN型またはI型の導電型を有する半導体層を
複数層形成し、その積層境界にて接合例えばPN
接合、PI接合、NI接合またはPIN接合を形成す
ることができる。
Furthermore, by connecting a plurality of reaction vessels, a plurality of semiconductor layers having conductivity type of P, N, or I can be formed, and junctions such as PN
A junction, PI junction, NI junction or PIN junction can be formed.

〔参考例1〕 基板支持体と一対のガイドによつて閉空間が形
成され、該閉空間内に保持された複数の基板に反
応性気体を基板の被形成面表面に概略平行に流
し、さらに一対の電極から電界を基板の被形成面
に概略平行に加える構成を有したプラズマ気相反
応装置を参考例として以下に示す。
[Reference Example 1] A closed space is formed by a substrate support and a pair of guides, a reactive gas is caused to flow approximately parallel to the surface of the substrate to be formed on a plurality of substrates held within the closed space, and A plasma vapor phase reaction apparatus having a configuration in which an electric field is applied from a pair of electrodes approximately parallel to the surface on which a substrate is formed will be shown below as a reference example.

第1図に従つて本参考例のプラズマ気相反応装
置を説明する。
The plasma vapor phase reactor of this reference example will be explained with reference to FIG.

この図面はPI接合、NI接合、PN接合、PIN接
合、PINIP接合PINIP接合またはPINPIN……
PIN接合等の基板上の半導体に異種導電型または
同種導電型でありながらも形成される半導体の主
成分または化学量論比の異なる半導体層をそれぞ
れの半導体をその前の工程において形成された半
導体層の影響を受けることを防ぐため、前の半導
体層を形成した反応容器に連設した他の独立した
反応容器で第2の半導体層を形成して、前の半導
体層上に積層して接合を作るとともに、さらに多
層に連続的に形成するための装置である。
This drawing shows PI junction, NI junction, PN junction, PIN junction, PINIP junction, PINIP junction or PINPIN...
Semiconductor layers with different conductivity types or the same conductivity type but with different main components or stoichiometric ratios are formed on a semiconductor on a substrate such as a PIN junction, and each semiconductor is a semiconductor formed in a previous process. In order to prevent the second semiconductor layer from being influenced by the previous semiconductor layer, a second semiconductor layer is formed in another independent reaction vessel connected to the reaction vessel in which the previous semiconductor layer was formed, and is laminated and bonded on top of the previous semiconductor layer. This is a device for creating and continuously forming multiple layers.

図面においては特にPIN接合を構成する3つの
P、IおよびN型の半導体層を積層して形成する
第1および第2の予備室を有するマルチチヤンバ
ー(ここでは3つの反応容器)方式のプラズマ気
相反応装置の装置例を示す。
In the drawings, a multi-chamber (in this case, three reaction vessels) type plasma having first and second preliminary chambers formed by laminating three P-, I-, and N-type semiconductor layers constituting a PIN junction is shown. An example of a gas phase reactor is shown.

図面における、、は3つの各反応容器
6,7,8を有し、それぞれ独立して反応性気体
の導入手段17,18,19と排気手段20,2
1,22とを有し、反応性気体が供給系または排
気系から逆流または他の系からの反応性気体の混
入を防いでいる。
In the drawings, , has three reaction vessels 6, 7, 8, each having independently reactive gas introduction means 17, 18, 19 and exhaust means 20, 2.
1 and 22 to prevent reactive gas from flowing back from the supply system or exhaust system or from mixing with reactive gas from other systems.

この装置は入口側には第1の予備室5が設けら
れ、とびら42より基板ホルダ(ホルダともい
う)74に基板4,4を挿着し、この予備室に配
置させた。この被形成面を有する基板は被膜形成
面を行なわない裏面を互いに接し、2〜10cm好ま
しくは3〜5cmの間隙を有して林立させている。
この間隙は基板の反応性気体の流れ方向の長さが
10cm、15cm、20cmと長くなるにつれて、3〜4
cm、4〜5cm、5〜6cmと広げた。さらにこの第
1の予備室5を真空ポンプ35にてバルブ34を
開けて真空引きをした。この後予め真空引きがさ
れている反応容器6,7,8にゲート弁44を閉
じることにより移動させたものである。この時反
応容器6に保持されていた基板1は反応容器7
に、また反応容器8に、また反応容器8に保持さ
れていた基板は第2の出口側の予備室9に同時に
ゲート弁45,46,47を開けて移動させた。
This apparatus was provided with a first preliminary chamber 5 on the entrance side, and substrates 4, 4 were inserted into a substrate holder (also referred to as holder) 74 through a door 42 and placed in this preliminary chamber. The substrates having the surfaces on which the film is to be formed are arranged such that the back surfaces on which the film is not formed are in contact with each other, with a gap of 2 to 10 cm, preferably 3 to 5 cm.
The length of this gap in the flow direction of the reactive gas on the substrate is
3 to 4 as the length increases to 10 cm, 15 cm, and 20 cm.
cm, 4-5 cm, and 5-6 cm. Furthermore, this first preliminary chamber 5 was evacuated using a vacuum pump 35 by opening a valve 34. Thereafter, the reaction vessels 6, 7, and 8, which had been evacuated in advance, were moved by closing the gate valve 44. At this time, the substrate 1 held in the reaction container 6 is transferred to the reaction container 7.
Then, the substrates held in the reaction vessel 8 and the substrates held in the reaction vessel 8 were simultaneously moved to the preliminary chamber 9 on the second outlet side by opening the gate valves 45, 46, and 47.

第2の予備室に移された基板はゲート弁47が
閉じられた後41より窒素が導入されて大気圧に
され、43のとびらより外に出した。
After the gate valve 47 was closed, the substrate transferred to the second preliminary chamber was brought to atmospheric pressure by introducing nitrogen through 41, and was taken out through the door 43.

即ちゲート弁の動きはとびら47,43が大気
圧で開けられた時はゲート弁44,45,46,
47は閉じられ、各チヤンバーにおいてはプラズ
マ気相反応が行なわれる。また逆にとびら42,
43が閉じられていて予備室5,9が十分真空引
きされた時は、ゲート弁44,45,46,47
が開き、各チヤンバーの基板、ホルダは隣りのチ
ヤンバーに移動する機構を有している。
That is, the movements of the gate valves are as follows: when the doors 47, 43 are opened at atmospheric pressure, the gate valves 44, 45, 46,
47 is closed, and a plasma gas phase reaction is carried out in each chamber. On the contrary, door 42,
43 is closed and the preliminary chambers 5, 9 are sufficiently evacuated, the gate valves 44, 45, 46, 47
It has a mechanism that opens and moves the substrate and holder of each chamber to the adjacent chamber.

さらに反応容器内に筒状空間を構成させ、その
筒状空間内に基板を設置してプラズマ反応により
基板上に被膜を形成するものであり、第1の反応
容器で被膜形成後は基板を配設しているホルダが
第2の反応容器に移動する構成となつている。第
2の反応容器では第1の反応容器と同様のホルダ
の上下をガイドによりとり囲み筒状空間を構成さ
せた。
Furthermore, a cylindrical space is formed in the reaction vessel, a substrate is placed in the cylindrical space, and a film is formed on the substrate by plasma reaction. After the film is formed in the first reaction vessel, the substrate is placed. The holder provided therein is configured to be moved to the second reaction vessel. In the second reaction vessel, a holder similar to that of the first reaction vessel was surrounded by guides at the top and bottom to form a cylindrical space.

そのため反応が筒状空間で行なわれると、第1
の反応室で基板上に形成した第1の膜と同様の膜
がホルダにも付着することになり、そのまま第2
の反応室にホルダを移動させて、さらに第2の膜
形成を行なうと、ホルダにも同様に第2の膜が形
成されることになる。従つてホルダには基板上に
膜形成を行なう時と同じ様な雰囲気で膜形成が行
なわれることになる。
Therefore, when the reaction takes place in a cylindrical space, the first
A film similar to the first film formed on the substrate in the reaction chamber will also adhere to the holder, and the second film will be deposited as is.
When the holder is moved to the reaction chamber and the second film is further formed, the second film is similarly formed on the holder. Therefore, the film is formed on the holder in the same atmosphere as when the film is formed on the substrate.

従つて本参考例の装置においてはホルダの内壁
には基板と同じように膜が形成されているため、
ホルダ内が膜形成面と同じような雰囲気となり、
例えホルダの内壁から第1の膜が離脱したとして
も、膜形成面でも同様なことが生じており、膜自
体の特性に影響を与える程度ではないため、良質
の膜を形成することができ、その結果良質の半導
体装置を作製することができます。さらにプラズ
マが筒状空間より外部にもれないため反応容器内
壁に膜形成がありません。このため反応容器内の
清掃が不要となります。
Therefore, in the device of this reference example, a film is formed on the inner wall of the holder in the same way as the substrate, so
The inside of the holder becomes the same atmosphere as the film formation surface,
Even if the first film detaches from the inner wall of the holder, the same thing will happen on the film forming surface, and it will not affect the properties of the film itself, so a high quality film can be formed. As a result, high quality semiconductor devices can be manufactured. Furthermore, since the plasma does not leak outside the cylindrical space, there is no film formation on the inner wall of the reaction vessel. This eliminates the need to clean the inside of the reaction vessel.

系における第1の反応容器6でのP型半導体
層を形成する場合を以下に記す。
The case of forming a P-type semiconductor layer in the first reaction vessel 6 in the system will be described below.

反応系(反応容器6を含む)は10-3〜10torr
好ましくは0.01〜1torr例えば0.1torrとした。
The reaction system (including reaction vessel 6) is 10 -3 to 10 torr
Preferably it is 0.01 to 1 torr, for example 0.1 torr.

反応性気体は珪化物気体24に対してはシラン
(SinH2o+2≧特にSiH4)、ジクロールシラン
(SiH2Cl1)、トリクロールシラン(SiHCl2)、四
フツ化珪素(SiF4)等があるが、取扱いが容易な
シランを用いた。価格的にはジクロールシランの
方が安価であり、これを用いてもよい。
For the silicide gas 24, reactive gases include silane (SinH 2o+2 ≧ especially SiH 4 ), dichlorosilane (SiH 2 Cl 1 ), trichlorosilane (SiHCl 2 ), and silicon tetrafluoride (SiF 4 ). Silane, which is easy to handle, was used. Dichlorosilane is cheaper and may be used.

本実施例のSixC1-x(0<X<1)を形成するた
め炭化物気体23に対してはメタン(CH4)を用
いた。CF4のような炭化物気体であつても、また
四塩化炭素(CCl4)のような塩化炭素であつて
もよい。
Methane (CH 4 ) was used for the carbide gas 23 to form SixC 1-x (0<X<1) in this example. It may be a carbide gas such as CF 4 or a carbon chloride such as carbon tetrachloride (CCl 4 ).

炭化珪素(SixC1-x0<X<1)に対しては、
P型の不純物としてボロンを水素にて2000PPM
に希釈されたジボランより25より供給した。ま
たガリユームをTMG(Ca(CH23)により1019
9×1021cm-3の濃度になるように加えてもよい。
For silicon carbide (SixC 1-x 0<X<1),
2000PPM of boron with hydrogen as a P-type impurity
diborane diluted to 25%. In addition, gallyum was treated with TMG (Ca(CH 2 ) 3 ) at 10 19 ~
It may be added to a concentration of 9×10 21 cm −3 .

キヤリアガス39は反応中は水素(H2)を用
いたが、反応開始の前後には窒素(N2)を液体
窒素により利用した。これらの反応性気体はそれ
ぞれの流量計33およびバルブ32をへて、反応
性気体の導入口17より高周波電源の負電極61
をへて反応容器6に供給された。反応性気体は7
0のガイドをへて筒状空間を構成する基板1およ
びホルダ74内に導入され、負電極61と正電極
51間を電気エネルギ例えば13.56MHzの高周波
エネルギを加えて反応せしめ、基板上に反応生成
物を被膜形成せしめた。
As the carrier gas 39, hydrogen (H 2 ) was used during the reaction, but nitrogen (N 2 ) was used in the form of liquid nitrogen before and after the start of the reaction. These reactive gases pass through the respective flowmeters 33 and valves 32, and then enter the negative electrode 61 of the high frequency power source from the reactive gas inlet 17.
The reactor was supplied to the reaction vessel 6 through the process. Reactive gas is 7
The substrate is introduced into the substrate 1 and the holder 74 forming a cylindrical space through a guide of 0, and electrical energy, for example, high frequency energy of 13.56 MHz, is applied between the negative electrode 61 and the positive electrode 51 to cause a reaction, and a reaction is generated on the substrate. The material was coated.

基板は100〜400℃例えば200℃に赤外線ヒータ
11,11′により加熱した。
The substrate was heated to 100-400°C, for example 200°C, by infrared heaters 11, 11'.

この赤外線ヒータは赤外線イメージ炉ともい
い、棒状を有するため上方のヒータを下方のヒー
タとが互いに直交する方向に配置して、この反応
容器内における特に筒状空間を200±10℃好まし
くは±50℃以内に設置した。このヒータは上側ま
たは下側のみでは反応性気体の流れ方向に200〜
120℃と80℃をも不均一を生じ、全く実用になら
なかつた。また互いに直交させることにより、基
板間の温度分布も±10℃以内とすることができ
た。この後、前記したが、この容器に前記した反
応性気体を導入し、さらに10〜50Wに高周波エネ
ルギ14を供給してプラズマ反応をおこさせた。
This infrared heater is also called an infrared image furnace, and since it has a rod shape, the upper heater and the lower heater are arranged in a direction orthogonal to each other, and the cylindrical space in this reaction vessel is heated to 200±10℃, preferably ±50℃. It was installed within ℃. This heater only has a 200~200°
Temperatures of 120°C and 80°C also caused non-uniformity and were not practical at all. Furthermore, by making the substrates orthogonal to each other, the temperature distribution between the substrates could be kept within ±10°C. Thereafter, as described above, the above-described reactive gas was introduced into the container, and high-frequency energy 14 of 10 to 50 W was further supplied to cause a plasma reaction.

かくしてP型半導体層はB2H6/SiH4=0.5%、
CH4/(SiH4+CH4)=0.5の条件にて、この反応
系で約100Åの厚さを有する薄膜として形成さ
せた。Eg=2.0eV、σ=1×10-4〜3×10-3(Ω
cm)-1であつた。
Thus, the P-type semiconductor layer has B 2 H 6 /SiH 4 =0.5%,
A thin film having a thickness of about 100 Å was formed using this reaction system under the conditions of CH 4 /(SiH 4 +CH 4 )=0.5. Eg=2.0eV, σ=1×10 -4 ~3×10 -3
cm) -1 .

従来炭化珪素は一般的に珪素のみに比べて大き
な高周波エネルギを必要とする。そのため、電界
が被形成面に垂直方向の場合、被形成面に設けら
れた透明導電膜(ITOまたは酸化スズの600〜800
Åの電極用被膜)はスパツタされて、酸化スズや
金属スズに変わつて透明ではなく白濁しやすい。
Conventional silicon carbide generally requires greater high frequency energy than silicon alone. Therefore, when the electric field is perpendicular to the surface to be formed, the transparent conductive film (ITO or tin oxide 600 to 800
When the electrode coating (A) is spattered, it turns into tin oxide or metal tin, which is not transparent and tends to become cloudy.

しかし本発明の実施例に示される如く、プラズ
マ電界を被形成面に概略平行にすると、この電界
による反応生成物は表面にそつて移動するため、
スパツタ効果による白濁化は30〜50W加えられて
も見られず、垂直電界の場合が2〜5wが限界だ
つたことに比べて、特性歩留りおよび製造歩留り
を向上させた。
However, as shown in the embodiments of the present invention, when the plasma electric field is made approximately parallel to the surface to be formed, the reaction products due to this electric field move along the surface.
No clouding due to sputtering effect was observed even when 30 to 50 W was applied, and the characteristic yield and manufacturing yield were improved compared to the case where the vertical electric field had a limit of 2 to 5 W.

基板は導体基板(ステンレス、チタン、窒化チ
タン、その他の金属)、半導体(珪素、炭化珪素、
ゲルマニユーム)、絶縁体(アルミナ、ガラス、
有機物質)または複合基板(ガラス絶縁基板上に
酸化スズ、ITO等の導電膜が単層またはITO上に
SnO2が形成された2層膜が形成されたもの、絶
縁基板上に選択的に導体電極が形成されたもの、
絶縁基板上にPまたはN型の半導体が形成された
もの)を用いた。基板は可曲性であつてもまた固
い板であつてもよい。
Substrates include conductor substrates (stainless steel, titanium, titanium nitride, and other metals), semiconductors (silicon, silicon carbide,
germanium), insulators (alumina, glass,
Organic materials) or composite substrates (conductive films such as tin oxide or ITO on a glass insulating substrate or a single layer on ITO)
One in which a two-layer film with SnO 2 is formed, one in which conductive electrodes are selectively formed on an insulating substrate,
A P- or N-type semiconductor formed on an insulating substrate was used. The substrate can be flexible or a rigid plate.

かくして1〜5分間プラズマ反応をさせて、P
型不純物としてホウ素またはガリユームが添加さ
れた炭化珪素膜を作製した。さらにこの第1の半
導体層上に基板を前記した操作順序に従つて第2
の反応容器7に移動し、ここで真性の半導体層を
約5000Åの厚さに形成させた。
In this way, a plasma reaction is performed for 1 to 5 minutes, and P
A silicon carbide film doped with boron or gallium as a type impurity was fabricated. Further, a substrate is placed on the first semiconductor layer and a second semiconductor layer is placed on top of the first semiconductor layer.
was moved to a reaction vessel 7, where an intrinsic semiconductor layer was formed to a thickness of about 5000 Å.

さらに高周波に加えて1GHz以上の周波数例え
ば2.45GHzのマイクロ波が供給されている。
Furthermore, in addition to high frequencies, microwaves with a frequency of 1 GHz or higher, for example 2.45 GHz, are supplied.

第2図において、反応性気体は66より導入さ
れ、石英管導入口より網状または多孔状の電極6
7をへて導出された。反応性気体の導出口18、
基板2、ホルダ74、排気口21、一対の電極6
7,68に相関関係については、第3にさらにそ
の斜視図(前半分を切断してある)で示してい
る。
In FIG. 2, the reactive gas is introduced from the quartz tube inlet into the mesh or porous electrode 6.
It was derived after going through 7. reactive gas outlet 18;
Substrate 2, holder 74, exhaust port 21, pair of electrodes 6
7 and 68 are further shown in a third perspective view (with the front half cut away).

即ち、第3図において基板2は裏面を互いに合
わせてさしこみ式になつたホルダ74に垂直方向
(鉛直方向)に互いに一定の間隙例えば3cmにて
平行に配置されている。ホルダと石英よりなり、
上側に円板状のデイスクとこれに連結した基板用
みぞ94を有している。デイスクは4つのサポー
タ80,80′により空間に保持され、サポータ
80,80′は軸79,79′の回転に従つて回転
し、その結果デイスクを3〜10回/分の速度で回
転し、反応性気体の均質化を促進させている。
That is, in FIG. 3, the substrates 2 are placed parallel to each other with a fixed gap of 3 cm, for example, in the vertical direction in a holder 74 which is an insert type with their back surfaces aligned with each other. Made of holder and quartz,
It has a disk-shaped disk on the upper side and a substrate groove 94 connected to the disk. The disk is held in space by four supports 80, 80', which rotate according to the rotation of the shafts 79, 79', thereby rotating the disk at a speed of 3 to 10 revolutions per minute; It promotes homogenization of reactive gases.

反応性気体は導出口18より1〜3mmの穴73
をへて網状電極(穴約5〜10mm)67をへて、下
方向にふき出させている。ホルダのガイド70に
より反応性気体の80方向への放出を防ぐため、
81の間隙は1cm以下好ましくは2〜5mmとし
た。そして反応性気体は基板2,2の被形成面お
よび基板2をたてるためのみぞ95を保持するた
めの壁96とによつて、筒状に構成した、即ち煙
突状に設けられた中空を83,85の方向に層状
に流させた。石英の側壁96はみぞ95より外側
に10〜20mm離れて設け、反応性気体の側壁96で
のみだれの発生を防ぎ、そのことにより基板2の
端部での被膜の膜厚を均一性をより促進させた。
The reactive gas is passed through a hole 73 with a diameter of 1 to 3 mm from the outlet 18.
It passes through a mesh electrode (hole approximately 5 to 10 mm) 67 and is blown out downward. In order to prevent reactive gas from being released in the 80 direction by the guide 70 of the holder,
The gap between 81 and 81 was 1 cm or less, preferably 2 to 5 mm. The reactive gas is formed into a cylindrical hollow space formed in the form of a chimney by the formation surfaces of the substrates 2, 2 and the wall 96 for holding the groove 95 for erecting the substrate 2. It was made to flow in layers in the directions of 83 and 85. The quartz sidewall 96 is spaced 10 to 20 mm outward from the groove 95 to prevent reactive gas from sagging on the sidewall 96, thereby increasing the uniformity of the coating thickness at the edge of the substrate 2. promoted.

また排気系に関しても、84からの反応性気体
の流入を少なくし、85を選択的に優先させるた
め、ガイド71と基板下端との間隙を1cm以下に
合わせて設けた。即ち82,84のガス流のコン
ダクタンスを83,85の約1/5以下好ましくは
1/30〜1/100にすることにより、筒状空間に選択
的に反応性気体を導き入れた。正電極68と基板
下端との距離はガイドの高さを調節して設けた。
Regarding the exhaust system, in order to reduce the inflow of reactive gas from 84 and to selectively give priority to 85, the gap between the guide 71 and the lower end of the substrate was set to 1 cm or less. That is, by setting the conductance of the gas flows 82 and 84 to about 1/5 or less, preferably 1/30 to 1/100, of 83 and 85, the reactive gas was selectively introduced into the cylindrical space. The distance between the positive electrode 68 and the lower end of the substrate was determined by adjusting the height of the guide.

さらに負電極67と基板上端即ちデイスク74
との距離も同様にガイド70により調節した。
Furthermore, the negative electrode 67 and the upper end of the substrate, that is, the disk 74
Similarly, the distance between the guide 70 and the guide 70 was adjusted.

第3図より明らかな如く、電極はその外周辺側
を石英のガイド70、上ぶた93、ガイド71、
下ぶた94によつて囲まれており、電極とチヤン
バー(特にステンレスチヤンバー)の内壁との寄
生放電の防止に努めた。さらに反応性気体の導入
口68の内径と負電極が概略同一の大きさを有
し、また排気口21内径と正電極とが概略同一の
大きさを有するため、高周波放電を行なうと、こ
の筒状空間即ち反応性気体の被形成面にそつて流
れて空間を優先的にプラズマ放電させている。そ
の結果、反応性気体のプラズマ化率がきわめて大
きくなり、ひいては反応容器(ベルジヤー)の内
壁に過剰の反応生成物がピンホール発生の原因と
なるフレーク状に付着してしまうことを防ぐこと
ができた。
As is clear from FIG. 3, the electrode has a quartz guide 70, an upper lid 93, a guide 71,
It is surrounded by a lower lid 94 to prevent parasitic discharge between the electrode and the inner wall of the chamber (particularly the stainless steel chamber). Furthermore, since the inner diameter of the reactive gas inlet 68 and the negative electrode have approximately the same size, and the inner diameter of the exhaust port 21 and the positive electrode have approximately the same size, when high-frequency discharge is performed, this cylinder The reactive gas flows along the shaped space, that is, the surface on which the reactive gas is formed, preferentially causing the space to become a plasma discharge. As a result, the plasma conversion rate of the reactive gas becomes extremely high, and it is possible to prevent excessive reaction products from adhering to the inner wall of the reaction vessel (belgear) in the form of flakes, which can cause pinholes. Ta.

以上の如き第3図の構成に加えて、その番号が
対応した第2図においては、赤外線ランプ12,
12′が上方向、下方向に設けられ、基板の均質
化を促進させている。
In addition to the configuration of FIG. 3 as described above, in FIG. 2 with corresponding numbers, infrared lamps 12,
12' are provided in the upper and lower directions to promote homogenization of the substrate.

第3図の構成は第1図における系、におけ
る反応容器6,8での電極、基板、基板支持体
(ホルダ)、反応性気体導出口、排気口においても
同様の構成を有せしめた。かくして第3図にいて
基板および基板支持体(ホルダ)は何らかの支障
なく77の系の方向より到り、また78の方向
の系の方向に移動させることができた。
The structure shown in FIG. 3 is similar to that of the electrodes, substrates, substrate supports (holders), reactive gas outlets, and exhaust ports in the reaction vessels 6 and 8 in the system shown in FIG. Thus, in FIG. 3, the substrate and the substrate support (holder) were able to arrive from the direction of the system 77 and move in the direction of the system 78 without any hindrance.

第2図における1GHz以上の周波数のマイクロ
波の効果に関しては、本発明人の出願になる特許
願57−126047(S57.7.19出願)に詳細が示されて
いる。
Regarding the effect of microwaves having a frequency of 1 GHz or higher in FIG. 2, details are shown in Patent Application No. 57-126047 (filed on July 19, 2013) filed by the present inventor.

図面では250℃において3Å/秒を高周波電界
を20Wとしてシランを30c.c./分加えると得ること
ができた。結果として従来の平行平板型の電極方
式において0.1〜1Å/秒に比べて、同一反応容
器において、例えば前者が10cm21まいであるのに
対し、10cm28まいを被膜の成長速度が従来も0.5
Å/秒とすると六倍になり、合計48倍の多量生産
が可能となつた。また従来50cmを作製する空間に
おいては、20cm×50cmの基板を間隙5cmとし、20
配列同時に可能となり、被形成面積は実質的に20
×50×20=2×104cm2と同様に8倍にすることが
でき、電極間距離は従来の4cmより25〜27cmにな
つたため、反応性気体のイオン化率も向上し、被
膜成長速度も4Å/秒を得ることができるため、
結果として64倍の成長速度を実質的に有するきわ
めて理想的な多量生産方式であることがわかつ
た。
In the drawing, it was possible to obtain 3 Å/sec at 250°C by applying a high frequency electric field of 20 W and silane at 30 c.c./min. As a result, compared to 0.1 to 1 Å/sec in the conventional parallel plate electrode system, the film growth rate in the same reaction vessel is 10 cm 2 8 Å/sec compared to 10 cm 2 8 Å/sec in the former case. 0.5
In terms of Å/second, this has increased six times, making it possible to produce a total of 48 times more volume. In addition, in the conventional space for manufacturing 50 cm, a 20 cm x 50 cm substrate with a gap of 5 cm,
Arraying can be done at the same time, and the area to be formed is practically 20
× 50 × 20 = 2 × 10 4 cm 2 , so it can be increased 8 times, and the distance between the electrodes is now 25 to 27 cm compared to the conventional 4 cm, which improves the ionization rate of reactive gas and increases the film growth rate. can also obtain 4 Å/s, so
As a result, it was found to be an extremely ideal mass production method with a growth rate that is 64 times faster.

かくして形成された半導体層は、プラズマ状態
の距離が長いため、光伝導度も2×10-4〜7×
10-3(Ωcm)-1、暗伝導度3×10-7〜1×10-1(Ω
cm)-1を有していた。
Since the semiconductor layer thus formed has a long plasma state distance, its photoconductivity also ranges from 2×10 -4 to 7×
10 -3 (Ωcm) -1 , dark conductivity 3×10 -7 ~1×10 -1
cm) -1 .

またかくして型半導体層を系にて約5000Å
の厚さに形成させた後、基板は前記した操作に従
つて系の反応容器8に移され、N型半導体層が
形成された。このN型半導体層には、第1図にお
いてフオスヒンをPH3/SiH4=0.1%とし31よ
りまたシランを30より、またキヤリアガスの水
素を29よりSiH4/H2=50として供給し系と
同様にして200Åの厚さにN型の微結晶系または
繊維構造を有す多結晶の半導体層を形成させたも
のである。その他反応装置については系と同様
である。
In this way, the type semiconductor layer is approximately 5000 Å thick in the system.
After forming the substrate to a thickness of , the substrate was transferred to the reaction vessel 8 of the system according to the operations described above, and an N-type semiconductor layer was formed. To this N-type semiconductor layer, as shown in FIG. 1, phosphin was supplied from 31 at PH 3 /SiH 4 =0.1%, silane was supplied from 30, and carrier gas hydrogen was supplied from 29 at SiH 4 /H 2 =50 to form a system. Similarly, an N-type microcrystalline or polycrystalline semiconductor layer having a fiber structure was formed to a thickness of 200 Å. Other reaction equipment is the same as the system.

かかる工程の後、第2の予備室9より外にPIN
接合を構成して出された基板上にアルミニユーム
電極を真空蒸着法により約1μmの厚さに作り、
ガラス基板上に(ITO+SnO2)表面電極−(PIN
半導体)(Al裏面電極)を構成させた。
After this process, enter the PIN from the second preliminary room 9.
An aluminum electrode with a thickness of approximately 1 μm is made by vacuum evaporation on the substrate that has been formed to form the bond.
(ITO + SnO 2 ) surface electrode - (PIN
Semiconductor) (Al back electrode) was constructed.

その光電変換装置としての特性は7〜9%平均
8%を10cm2の基板でAM1(100mW/cm2)にて真
性効率特性として有し、ハイブリツド型にした15
cm×40cmの基板においても、6〜7%を真性効率
で得ることができた。この効率の向上は光が入射
する側のPI接合がきわめて面的に構成され、ま
たアモルフアス半導体またはセミアモルフアス半
導体等の非単結晶半導体においても、P型半導体
層上にI型半導体層を成長積層させたことによる
もので、また解放電圧は0.88〜0.9Vであつたが、
短絡電流は20〜22mA/cm2と大きく、またFFも
0.70〜0.78と大きく、PIN型の半導体層内部にお
ける再結合中心の密度が従来の方法に比べ1/10〜
1/50になつたことによる電流増加が大きな特性改
良につながつたものと推定される。
Its characteristics as a photoelectric conversion device are 7 to 9%, with an average of 8% as an intrinsic efficiency characteristic at AM1 (100 mW/cm 2 ) on a 10 cm 2 substrate, and it is a hybrid type 15
Even on a cm×40 cm substrate, an intrinsic efficiency of 6 to 7% could be obtained. This improvement in efficiency is due to the fact that the PI junction on the side where light enters is extremely planar, and even in non-single crystal semiconductors such as amorphous or semi-amorphous semiconductors, an I-type semiconductor layer is grown on a P-type semiconductor layer. This was due to the lamination, and the release voltage was 0.88 to 0.9V.
The short circuit current is large at 20 to 22 mA/ cm2 , and the FF is also
As large as 0.70 to 0.78, the density of recombination centers inside the PIN type semiconductor layer is 1/10 to 1/10 compared to conventional methods.
It is estimated that the increase in current due to the reduction to 1/50 led to a large improvement in characteristics.

かくの如く本参考例のプラズマ反応装置は形成
される半導体において生産性を30〜70倍も向上さ
せ、また特性も従来の5〜7%の変換効率に比べ
30%も向上させるきわめて独創的なものである。
As described above, the plasma reactor of this reference example improves the productivity of semiconductors formed by 30 to 70 times, and the characteristics are also improved compared to the conventional conversion efficiency of 5 to 7%.
This is an extremely original product that improves performance by 30%.

〔参考例2〕 本参考例は基板の配置方法を変えた例である。[Reference example 2] This reference example is an example in which the method of arranging the substrates is changed.

本参考例は第5図にその構造を示すものであ
り、第5図Aは第3図に示す構造に対応させたも
のである。
The structure of this reference example is shown in FIG. 5, and FIG. 5A corresponds to the structure shown in FIG. 3.

第5図Aにおいて反応性気体の導入口66より
18、負電極67をへて排気口21、正電極6
8、排気系74に至るが、基板2はテーパ状を有
し、基板の導入口側より排気口側に向かつてせま
くなり、その形成される膜の均一化をさらに促進
させたものである。
In FIG. 5A, the reactive gas is introduced from the inlet 66 to the exhaust port 21 via the negative electrode 67, and then to the positive electrode 6.
8. As for the exhaust system 74, the substrate 2 has a tapered shape and becomes narrower from the inlet side to the exhaust port side of the substrate, further promoting uniformity of the formed film.

ここでAにおいてはフレークが被形成面に付く
ことがなく、即ちピンホールによる製造歩留りも
向上し、加えて被膜の膜質も反応性気体の流れ方
向において均質な結果を得た。しかし第1の製造
装置に比べてその生産性は約1/2になつてしまつ
た。
Here, in A, flakes were not attached to the surface to be formed, that is, the production yield due to pinholes was improved, and in addition, the film quality of the film was homogeneous in the flow direction of the reactive gas. However, the productivity was about 1/2 that of the first manufacturing equipment.

以上の明細書中においては、PIN接合を1つ有
するものとした。しかしPINIP型フオトトランジ
スタ、PINPIN……PINのタンデム構造の光電変
換装置等の多くの応用もその半導体層の数に従つ
て反応容器をさらに連結すればよい。
In the above specification, it is assumed that there is one PIN junction. However, in many applications such as PINIP type phototransistors, PINPIN...PIN tandem structure photoelectric conversion devices, reaction vessels may be further connected according to the number of semiconductor layers.

以上の説明において、形成される非単結晶半導
体被膜中の結晶構造がアモルフアスであれ多結晶
であれ、その構造には制限を受けない。
In the above description, there is no restriction on the crystal structure of the formed non-single crystal semiconductor film, whether it is amorphous or polycrystalline.

さらにこの珪素または炭素の不対結合手を水素
によりSi−H、C−Hにて中和するのではなくSi
−Cl、C−Clとハロゲン化物特に塩化物性気体を
用いて実施してもよいことはいうまでもなく、こ
の濃度は10原子%以下、例えば2〜5原子%がこ
のましかつた。
Furthermore, instead of neutralizing the dangling bonds of silicon or carbon with hydrogen by Si-H or C-H,
It goes without saying that the process may be carried out using -Cl, C-Cl and a halide gas, particularly a chloride gas, but the concentration is preferably 10 at % or less, for example 2 to 5 at %.

また形成させる半導体の種類に関しては、族
のSi、Ge、SixC1-x(0<X<1)、SixGe1-x(0
<X<1)、SixSn1-x(0<X<1)のみではな
く、これ以外にGaAs、GaAlAs、BP、Cds等の
化合物半導体であつてもよいことはいうまでもな
い。
Regarding the types of semiconductors to be formed, Si, Ge, SixC 1-x (0<X<1), SixGe 1-x (0
<X<1), SixSn 1-x (0<X<1), but it goes without saying that compound semiconductors such as GaAs, GaAlAs, BP, and Cds may also be used.

また形成された炭化珪素被膜に対しフオトエツ
チング技術を用いて選択的にPまたはN型の不純
物を混入または拡散してPN接合を部分的に作
り、この接合を利用してトランジスタ、ダイオー
ド、W−N−W(WIDE−NALLOW−WIDE)構
造のPIN接合型の可視光レーザ、発光素子または
光電変換素子を作つてもよい。特に光入射光側の
エネルギバンド巾を大きくしたヘテロ接合構造を
有するW−N(WIDE TO NALLOW)と各反応
室にて導電型のみではなく生成物を異ならせてそ
れぞれ独立して作製して積層をさせることが可能
となり、工業的にきわめて重要なものであると信
ずる。
In addition, P- or N-type impurities are selectively mixed or diffused into the formed silicon carbide film using photoetching technology to partially create a PN junction, and this junction is used to create transistors, diodes, W- A PIN junction type visible light laser, light emitting element, or photoelectric conversion element having an N-W (WIDE-NALLOW-WIDE) structure may be made. In particular, W-N (WIDE TO NALLOW), which has a heterojunction structure with a wide energy band width on the incident light side, is fabricated independently and laminated with different conductivity types as well as different products in each reaction chamber. We believe that this technology is extremely important industrially.

〔発明の効果〕〔Effect of the invention〕

複数の基板全体をかこむ構造の基板支持体と一
対のガイドによつて複数の基板を閉空間に閉じ込
め、しかも基板の被形成面に平行に反応性気体と
電界を加えることによつて、複数の基板に対し同
時に成膜を行うことができ、高い生産性を得るこ
ととができるようになつた。
By confining multiple substrates in a closed space using a substrate support with a structure surrounding the entire multiple substrates and a pair of guides, and applying a reactive gas and an electric field parallel to the surface of the substrate to be formed, multiple substrates can be formed. It has become possible to simultaneously form films on substrates and obtain high productivity.

さらに成膜中において基板支持体にプラズマが
閉じ込められるので、反応容器内に不用な成膜を
することが少なくなり、CVDプロセスにおいて
問題となる反応容器内のクリーニングの問題を低
減することができた。
Furthermore, since the plasma is confined within the substrate support during film formation, unnecessary film formation within the reaction vessel is reduced, reducing the problem of cleaning inside the reaction vessel, which is a problem in the CVD process. .

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

第1図、第2図は参考例の半導体膜形成用製造
装置の概略図を示す。第3図は第2図の装置の一
部の斜視図を示す。第4図は本発明の実施例を示
す。第5図は第3図に対応した他の参考例を示
す。 〔符号の説明〕、26,27,28……気体導
入系、66……導入口、18……導出口、21…
…排出口、76……排気系、37……ロータリー
ポンプ、74……基板支持体、70,71……反
応性気体、15……高周波電源、67,72……
一対の電極、12,12′……赤外線ランプ。
FIGS. 1 and 2 are schematic diagrams of a manufacturing apparatus for forming a semiconductor film as a reference example. FIG. 3 shows a perspective view of a portion of the apparatus of FIG. FIG. 4 shows an embodiment of the invention. FIG. 5 shows another reference example corresponding to FIG. 3. [Explanation of symbols], 26, 27, 28... gas introduction system, 66... inlet, 18... outlet, 21...
...Exhaust port, 76...Exhaust system, 37...Rotary pump, 74...Substrate support, 70, 71...Reactive gas, 15...High frequency power supply, 67, 72...
A pair of electrodes, 12, 12'...infrared lamp.

Claims (1)

【特許請求の範囲】 1 反応性気体を導入する手段及び排出する手段
と、 一対の電極と、 一対のガイドと、 前記一対の電極間に複数の基板を被形成面を離
間して保持する手段と、 前記複数の基板全体を囲む構造の移動可能な基
板支持体と、 を有したプラズマ気相反応装置であつて 前記一対のガイドと前記基板支持体とにより、
前記複数の基板は閉空間に閉じ込められ、 反応性気体が前記基板の被形成面に対し概略平
行に流れるように、前記反応性気体を導入する手
段及び排出する手段とが設けられ、 前記一対の電極から印加されるプラズマを生じ
せしめる電界が前記基板の被形成面に対し概略平
行に加えられるように、前記一対の電極は設けら
れ、 前記反応性気体の流れと前記プラズマを生じせ
しめる電界とが互いに概略直交するように、前記
反応性気体を導入する手段及び排出する手段と、
前記一対の電極とが設けられ、 ていることを特徴とするプラズマ気相反応装置。 2 反応性気体を導入する手段及び排出する手段
と、 一対の電極と、 一対のガイドと、 前記一対の電極間に複数の基板を被形成面を離
間して保持する手段と、 前記複数の基板全体をかこむ構造の移動可能な
基板支持体と、 を有したプラズマ気相反応装置を用いたプラズマ
気相反応装置であつて、 基板は、前記一対のガイドと前記基板支持体と
により、閉空間に閉じ込められており、 反応性気体は前記基板の被形成面に対し概略平
行に流され、 前記一対の電極から印加されるプラズマを生じ
せしめる電界は前記基板の被形成面に対して概略
平行に加えられ、 かつ、前記反応性気体の流れと前記プラズマを
生じせしめる電界が互いに概略直交するようにし
てプラズマ気相反応を行う、 ことを特徴とするプラズマ気相反応方法。
[Claims] 1. means for introducing and discharging a reactive gas, a pair of electrodes, a pair of guides, and a means for holding a plurality of substrates between the pair of electrodes with the surfaces to be formed separated from each other. and a movable substrate support having a structure surrounding the entire plurality of substrates, the plasma vapor phase reactor comprising: the pair of guides and the substrate support,
The plurality of substrates are confined in a closed space, and means for introducing and discharging the reactive gas are provided so that the reactive gas flows approximately parallel to the surface on which the substrate is formed; The pair of electrodes are provided so that the electric field that generates the plasma applied from the electrodes is applied approximately parallel to the surface on which the substrate is formed, and the flow of the reactive gas and the electric field that generates the plasma are connected. means for introducing the reactive gas and means for discharging the reactive gas so as to be substantially perpendicular to each other;
A plasma vapor phase reaction apparatus, characterized in that the pair of electrodes are provided. 2 means for introducing and discharging reactive gas; a pair of electrodes; a pair of guides; a means for holding a plurality of substrates between the pair of electrodes with their formation surfaces separated; and the plurality of substrates. A plasma vapor phase reactor using a plasma vapor phase reactor having a movable substrate support having a structure surrounding the entire structure, wherein the substrate is moved into a closed space by the pair of guides and the substrate support. The reactive gas is flowed approximately parallel to the formation surface of the substrate, and the electric field for generating plasma applied from the pair of electrodes is approximately parallel to the formation surface of the substrate. and performing the plasma vapor phase reaction in such a manner that the flow of the reactive gas and the electric field that generates the plasma are substantially perpendicular to each other.
JP63292203A 1988-11-18 1988-11-18 Plasma vapor reaction Granted JPH01157520A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63292203A JPH01157520A (en) 1988-11-18 1988-11-18 Plasma vapor reaction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63292203A JPH01157520A (en) 1988-11-18 1988-11-18 Plasma vapor reaction

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP57163730A Division JPS5952835A (en) 1982-09-20 1982-09-20 Plasma vapor reactor

Publications (2)

Publication Number Publication Date
JPH01157520A JPH01157520A (en) 1989-06-20
JPH0522376B2 true JPH0522376B2 (en) 1993-03-29

Family

ID=17778864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63292203A Granted JPH01157520A (en) 1988-11-18 1988-11-18 Plasma vapor reaction

Country Status (1)

Country Link
JP (1) JPH01157520A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW237562B (en) 1990-11-09 1995-01-01 Semiconductor Energy Res Co Ltd
JP3255942B2 (en) 1991-06-19 2002-02-12 株式会社半導体エネルギー研究所 Method for manufacturing inverted staggered thin film transistor
FI128855B (en) * 2019-09-24 2021-01-29 Picosun Oy Fluid distributing device for a thin-film deposition apparatus, related apparatus and methods

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5578524A (en) * 1978-12-10 1980-06-13 Shunpei Yamazaki Manufacture of semiconductor device
JPS5731130A (en) * 1980-07-31 1982-02-19 Matsushita Electric Ind Co Ltd Method and device for plasma chemical vapour deposition

Also Published As

Publication number Publication date
JPH01157520A (en) 1989-06-20

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