JPH03214724A - Thin-film manufacturing method - Google Patents

Thin-film manufacturing method

Info

Publication number
JPH03214724A
JPH03214724A JP2009799A JP979990A JPH03214724A JP H03214724 A JPH03214724 A JP H03214724A JP 2009799 A JP2009799 A JP 2009799A JP 979990 A JP979990 A JP 979990A JP H03214724 A JPH03214724 A JP H03214724A
Authority
JP
Japan
Prior art keywords
raw material
gas
gases
material gases
thin film
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
JP2009799A
Other languages
Japanese (ja)
Other versions
JP2555209B2 (en
Inventor
Takashi Yoshida
隆 吉田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Corporate Research and Development 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 Fuji Electric Corporate Research and Development Ltd filed Critical Fuji Electric Corporate Research and Development Ltd
Priority to JP2009799A priority Critical patent/JP2555209B2/en
Publication of JPH03214724A publication Critical patent/JPH03214724A/en
Application granted granted Critical
Publication of JP2555209B2 publication Critical patent/JP2555209B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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)

Abstract

PURPOSE:To enable each of a plurality of types of raw material gases to be dissociated under optimum conditions by passing the raw material gases to be introduced into a reaction bath through an independently temperature- controlled conduit. CONSTITUTION:When producing a thin film by dissolving a reaction gas obtained by mixing a plurality of raw material gases 41 and 42 within a reaction bath 1 for depositing a degradation generated object, at least one raw material gas is introduced into the reaction bath 1 through independently temperature- controlled conduits 51 and 52, thus giving a dissociation energy which is optimum to the raw material gas and generating a radical which is best suited for film formation. Thus, even if raw material gases, where a plurality types of raw material gases are mixed, are cracked, generation of an undesirable radical, etc., can be prevented, dissociation can be made under optimum conditions, and the film quality of the thin film can be improved.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、非品質シリコン太陽電池や非晶質シリコン薄
膜トランジスタなどの材料となる非晶質シリコン系薄膜
のような薄膜の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for manufacturing thin films such as amorphous silicon-based thin films that are used as materials for non-quality silicon solar cells, amorphous silicon thin film transistors, and the like.

〔従来の技術〕[Conventional technology]

最近、特に半導体工業の分野で薄膜の利用分野が拡大し
ている。そのような薄膜としては、非品質シリコン,多
結晶シリコン,酸化シリコンあるいは窒化シリコンなど
の薄膜がある。薄膜の製造方法としてはCVD技術を用
いるのが一般的で、原料化合物ガスに解離エネルギーを
与え、分解生成物からなる所期の組成の薄膜を堆積させ
るものである。例えば非品質シリコン系薄膜の製造方法
としては、シラン系原料ガスのガス分子を、プラズマ放
電、熱エネルギーあるいはレーザ,紫外線等の光を用い
て励起し、分解させて基板上に堆積し、薄膜を形成する
方法が知られている。
Recently, the field of application of thin films has been expanding, especially in the field of semiconductor industry. Such thin films include thin films of non-quality silicon, polycrystalline silicon, silicon oxide or silicon nitride. CVD technology is generally used as a method for manufacturing thin films, in which dissociation energy is applied to a raw material compound gas to deposit a thin film of a desired composition made of decomposition products. For example, a method for producing a non-quality silicon-based thin film is to excite gas molecules of a silane-based raw material gas using plasma discharge, thermal energy, laser, ultraviolet light, or other light, decompose them, and deposit them on a substrate to form a thin film. Methods of forming are known.

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

薄膜の材料にシリコン以外の元素を添加し、所望の光学
バンドギャップを有する非品質材料として、a−SiG
e:Hやa−SiC:Hなどの化合物半導体とする場合
には、原料ガスとしてシラン(SiH*)のほかに、ゲ
ルマン(GeH*) ,メタン(CH*)などを用いる
。また、非品質材料にほう素や燐などのドーピングを行
う場合、ジボラン(BJa)やフォスフィン(PHs)
を反応ガスに添加する。このような異種の原料ガスを混
合した反応ガスを用いる場合、原料ガスのうち最も分解
しにくいガスに対してそれが分解できるように原料ガス
分解のエネルギーを与える。このため、分解エネルギー
の低いガスなどは、最適条件での解離ができず、好まし
くないラジカル等を発生することが問題となっていた。
A-SiG is a non-quality material that has a desired optical band gap by adding elements other than silicon to the thin film material.
In the case of forming a compound semiconductor such as e:H or a-SiC:H, germane (GeH*), methane (CH*), etc. are used in addition to silane (SiH*) as a raw material gas. In addition, when doping non-quality materials with boron, phosphorus, etc., diborane (BJa) and phosphine (PHs)
is added to the reaction gas. When using a reaction gas that is a mixture of such different types of raw material gases, energy for decomposing the raw material gases is given to the gas that is the most difficult to decompose among the raw material gases so that it can be decomposed. For this reason, gases with low decomposition energy cannot be dissociated under optimal conditions, resulting in the generation of undesirable radicals and the like.

本発明の目的は、複数の種類の原料ガスのそれぞれを最
適条件で解離させる薄膜製造方法を提供することにある
An object of the present invention is to provide a thin film manufacturing method that dissociates each of a plurality of types of raw material gases under optimal conditions.

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

上記の目的を達成するために、本発明は、複数の原料ガ
スを混合してなる反応ガスを反応槽内で分解して分解生
成物を堆積させる薄膜製造方法において、少なくとも一
つの原料ガスを独立して温度制御した導管を通じて反応
槽内へ導入するものとする。
In order to achieve the above object, the present invention provides a thin film manufacturing method in which a reaction gas obtained by mixing a plurality of raw material gases is decomposed in a reaction tank and decomposition products are deposited, in which at least one raw material gas is It shall be introduced into the reaction tank through a temperature-controlled conduit.

〔作用〕[Effect]

解離エネルギーの異なる原料ガスを独立して温度制御し
た導管を通すことによりその原料ガスに最適な解離エネ
ルギーを与え、最も膜形成に適したラジカルを発生させ
ることができる。従って、複数の種類の原料ガスを混合
してなる原料ガスを分解する場合も、好ましくないラジ
カル等の発生が防止され、健全な薄膜が形成される。
By passing raw material gases with different dissociation energies through conduits whose temperatures are independently controlled, the optimal dissociation energy can be given to the raw material gases, and radicals most suitable for film formation can be generated. Therefore, even when decomposing a raw material gas made by mixing a plurality of types of raw material gases, generation of undesirable radicals etc. is prevented and a healthy thin film is formed.

〔実施例〕〔Example〕

以下、図を引用して本発明の実施例について説明する。 Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の一実施例のための装置を示し、キャリ
アガス導入口11とガス排気口12を有する真空槽(反
応槽)1の内部に、基板温度制御用ヒータ2が設けられ
、その上に基板3が設置されている。この基板に対して
、複数のガス導入口41.42から、つながれた原料ガ
ス反応管51.52を通して2種類の原料ガスが吹き付
けられる。原料ガス反応管51 . 52は保護カバー
6に覆われ、反応管温度制御用ヒータ7によって任意の
温度に制御可能のため、この内部を通る原料ガスの解離
を自由に制御することが可能である。この装置を用いる
ことにより、例えば、シランとゲルマンといった解離エ
ネルギーの異なる2種類のガスから非品質シリコンゲル
マンのようなアロイ半導体を形成する場合、2種類のガ
スを別々の原料ガス反応管51.52より真空槽1に導
入し、別々の最適温度でガスを解離することが出来る。
FIG. 1 shows an apparatus for an embodiment of the present invention, in which a substrate temperature control heater 2 is provided inside a vacuum chamber (reaction chamber) 1 having a carrier gas inlet 11 and a gas exhaust port 12. A substrate 3 is placed on top of it. Two types of raw material gases are blown onto this substrate from a plurality of gas introduction ports 41.42 through connected raw material gas reaction tubes 51.52. Raw material gas reaction tube 51. 52 is covered with a protective cover 6 and can be controlled to an arbitrary temperature by a reaction tube temperature control heater 7, so that it is possible to freely control the dissociation of the raw material gas passing through the inside. By using this apparatus, for example, when forming an alloy semiconductor such as non-quality silicon germane from two types of gases such as silane and germane having different dissociation energies, the two types of gases can be separated into separate source gas reaction tubes 51 and 52. The gases can be introduced into the vacuum chamber 1 and dissociated at different optimum temperatures.

これにより、各々のガスから最も膜形成に適したラジカ
ルを発生可能なため、例えば、シランの解離温度を90
0〜1200℃に、ゲルマンの解離温度を600〜80
0℃に制御した場合には、その原料ガスの流量比を制御
することにより第2図に示すように、光学バンドギャッ
プEgで1.3〜1 . 7eVの範囲で104〜10
−’ S/cI1の光伝導度σph、かつ5桁以上の光
暗伝導度比σph/σdを持ったシリコンゲルマン膜を
形成可能である。このとき、キャリアガス導入口11か
らはキャリアガスとして水素を流して真空槽中に層流を
形成している。原料ガスを、シランとメタンに変えれば
シリコンカーバイトの作成が、シランとアンモニアに変
えれば、窒化シリコンの形成も可能である。キャリアガ
スの種類はHeやN8などのガスを用いることも可能で
ある。また、3源の原料ガスから膜形成を行う場合、す
なわち、シリコンゲルマンやシリコンカーバイト等にド
ーピングを行う場合等には原料ガス反応管を3本用いれ
ばよい。
This makes it possible to generate radicals most suitable for film formation from each gas, so for example, the dissociation temperature of silane can be set to 90°C.
0-1200℃, germane dissociation temperature 600-80℃
When the temperature is controlled at 0°C, by controlling the flow rate ratio of the raw material gas, the optical bandgap Eg is 1.3 to 1.3°C, as shown in FIG. 104-10 in the 7eV range
-' It is possible to form a silicon germane film having a photoconductivity σph of S/cI1 and a photodark conductivity ratio σph/σd of 5 digits or more. At this time, hydrogen is flowed as a carrier gas from the carrier gas inlet 11 to form a laminar flow in the vacuum chamber. By changing the raw material gases to silane and methane, it is possible to create silicon carbide, and by changing the raw material gases to silane and ammonia, it is also possible to form silicon nitride. As the type of carrier gas, it is also possible to use gases such as He and N8. Further, when forming a film from three source gases, that is, when doping silicon germane, silicon carbide, etc., three source gas reaction tubes may be used.

第3図は本発明の別の実施例のための装置を示す断面図
で、第1図の装置と異なる点は、原料ガス反応管51.
52を加熱している反応管温度制御用ヒータ部7を囲む
保護カバー6が予備排気ボート61から排気されている
点と、2本の原料ガス反応管51 . 52の間に熱反
射板62が設けられている点である。ヒータ部を別排気
としたのでヒータからの不純物混入が防止可能で、しか
も熱反射板62を設けたことにより反応管温度制御用ヒ
ータ7の温度制御の独立性が大きく向上した。
FIG. 3 is a sectional view showing an apparatus according to another embodiment of the present invention, which differs from the apparatus shown in FIG. 1 in that the source gas reaction tube 51.
The protective cover 6 surrounding the reaction tube temperature control heater section 7 that heats the reaction tubes 52 is exhausted from the preliminary exhaust boat 61, and the two raw material gas reaction tubes 51. 52 is that a heat reflecting plate 62 is provided between them. Since the heater section was separately vented, it was possible to prevent contamination of impurities from the heater, and by providing the heat reflecting plate 62, the independence of temperature control of the heater 7 for controlling the temperature of the reaction tube was greatly improved.

第4図は、本発明のさらに別の実施例のための装置を示
すもので、第一の原料ガス導入口41と第二の原料ガス
導入口42ならびに排気口12を有する真空槽1の中に
第一の原料ガス導入口41に反応管温度制御用ヒータ7
を有する原料ガス反応管51が接続され、さらにその先
には、RFまたはDC電極8が設置されている。この電
極と対向する形でヒータ71を有するサセプタ21が設
置され、その上部の基板3上には、原料ガス反応管51
を通過し解離したガスと、第二の原料ガス導入口42を
通して供給されるガスを原料としてのプラズマCVDに
より薄膜が形成される。例えば、原料ガスとしてシラン
,メタン,ジポラン,水素を用いてP型のa−SiC:
H膜を製造する場合、水素希釈したジボランを原料ガス
反応管51を通して供給することにより、ほう素の分解
比率を大幅に向上させることが可能である。反応管51
の温度を例えば500〜1000℃に加熱すると、第5
図の●で示すように従来のプラズマCVDO例○に比較
して1桁以上ほう素の活性化度を向上させることができ
る。この他にも、2種類以上のガスを反応させたい場合
には第二の原料ガス反応管を設ければ良い。なお、この
実施例はプラズマCVDと熱CVDを組合わせたもので
あるが、光CVDと熱CVDを組合わせてもよい。
FIG. 4 shows an apparatus for yet another embodiment of the present invention, in which the interior of a vacuum chamber 1 having a first raw material gas inlet 41, a second raw material gas inlet 42, and an exhaust port 12 is shown. A heater 7 for controlling the temperature of the reaction tube is connected to the first raw material gas inlet 41.
A raw material gas reaction tube 51 having a diameter is connected thereto, and an RF or DC electrode 8 is installed beyond that. A susceptor 21 having a heater 71 is installed to face this electrode, and a source gas reaction tube 51 is placed on the substrate 3 above the susceptor 21.
A thin film is formed by plasma CVD using gas dissociated by passing through and gas supplied through the second raw material gas inlet 42 as raw materials. For example, P-type a-SiC using silane, methane, diporane, and hydrogen as raw material gases:
When producing an H film, by supplying diborane diluted with hydrogen through the raw material gas reaction tube 51, it is possible to significantly improve the boron decomposition ratio. Reaction tube 51
For example, when heating the temperature to 500-1000℃, the fifth
As shown by ● in the figure, the activation degree of boron can be improved by more than one order of magnitude compared to the conventional plasma CVDO example ○. In addition, if two or more types of gases are desired to react, a second source gas reaction tube may be provided. Although this embodiment combines plasma CVD and thermal CVD, optical CVD and thermal CVD may also be combined.

各装置の原料ガス反応管には、高温に耐え、かつ不純物
を放出しない材料が必要で、石英,シリコンカーバイト
.アルミナ等の材料を用いる。
The raw material gas reaction tubes of each device must be made of materials that can withstand high temperatures and do not release impurities, such as quartz or silicon carbide. A material such as alumina is used.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、反応槽内に導入する原料ガスを独立に
温度制御された導管を通すことにより、それぞれのガス
に必要な解離エネルギーを与え、最適な条件で分解を行
うことが可能となった。このため、解離エネルギーの異
なる原料ガスの分解を独立に制御し、それぞれの原料ガ
スから堆積する成分元素からなるアロイ半導体などのm
sの膜質を向上させることができた。
According to the present invention, by passing the raw material gases introduced into the reaction tank through independently temperature-controlled conduits, it is possible to give each gas the necessary dissociation energy and perform decomposition under optimal conditions. Ta. For this reason, it is possible to independently control the decomposition of raw material gases with different dissociation energies, and to produce composite materials such as alloy semiconductors made of component elements deposited from each raw material gas.
The film quality of s could be improved.

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

第1図は本発明の一実施例のための装置の断面図、第2
図は第1図の装置で製造されたシリコンゲルマン膜の光
暗伝導度と光学バンドギャップとの関係線図、第3図,
第4図はそれぞれ本発明の異なる実施例のための装置の
断面図、第5図は第4図の装置で製造されたa−SiC
:H膜の特性とジボランガス添加量との関係線図である
。 1:真空槽、3:基板、41,42:原料ガス導入口、
51.52F原料ガス反応管、7:ヒータ。
FIG. 1 is a sectional view of an apparatus for one embodiment of the present invention;
The figure shows the relationship between the optical dark conductivity and the optical bandgap of the silicon germane film produced using the apparatus shown in Figure 1, and Figure 3.
4 is a cross-sectional view of an apparatus for different embodiments of the present invention, and FIG. 5 is a-SiC manufactured with the apparatus of FIG. 4.
: It is a relationship diagram between the characteristics of the H film and the amount of diborane gas added. 1: Vacuum chamber, 3: Substrate, 41, 42: Raw material gas inlet,
51.52F raw material gas reaction tube, 7: Heater.

Claims (1)

【特許請求の範囲】[Claims] 1)複数の原料ガスを混合してなる反応ガスを反応槽内
で分解して分解生成物を堆積させる薄膜製造方法におい
て、少なくとも一つの原料ガスを独立して温度制御した
導管を通じて反応槽内に導入することを特徴とする薄膜
製造方法。
1) In a thin film manufacturing method in which a reaction gas formed by mixing multiple raw material gases is decomposed in a reaction tank and decomposition products are deposited, at least one raw material gas is introduced into the reaction tank through an independently temperature-controlled conduit. A thin film manufacturing method characterized by introducing.
JP2009799A 1990-01-19 1990-01-19 Thin film manufacturing method Expired - Fee Related JP2555209B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009799A JP2555209B2 (en) 1990-01-19 1990-01-19 Thin film manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009799A JP2555209B2 (en) 1990-01-19 1990-01-19 Thin film manufacturing method

Publications (2)

Publication Number Publication Date
JPH03214724A true JPH03214724A (en) 1991-09-19
JP2555209B2 JP2555209B2 (en) 1996-11-20

Family

ID=11730244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009799A Expired - Fee Related JP2555209B2 (en) 1990-01-19 1990-01-19 Thin film manufacturing method

Country Status (1)

Country Link
JP (1) JP2555209B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5500047A (en) * 1994-11-23 1996-03-19 Electronics & Telecommunications Research Institute Apparatus for adsorbing atomic hydrogen on surface
US5535048A (en) * 1988-09-15 1996-07-09 Flamel Technologies Nonlinearly optically active compounds
JP2006294608A (en) * 2005-04-06 2006-10-26 Samsung Sdi Co Ltd Method for manufacturing organic electroluminescent device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59185828U (en) * 1983-05-30 1984-12-10 沖電気工業株式会社 semiconductor manufacturing equipment
JPS61284931A (en) * 1985-06-11 1986-12-15 Fujitsu Ltd Vapor growth equipment
JPS63197324A (en) * 1987-02-12 1988-08-16 Seiko Instr & Electronics Ltd Gas source cell

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59185828U (en) * 1983-05-30 1984-12-10 沖電気工業株式会社 semiconductor manufacturing equipment
JPS61284931A (en) * 1985-06-11 1986-12-15 Fujitsu Ltd Vapor growth equipment
JPS63197324A (en) * 1987-02-12 1988-08-16 Seiko Instr & Electronics Ltd Gas source cell

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5535048A (en) * 1988-09-15 1996-07-09 Flamel Technologies Nonlinearly optically active compounds
US5500047A (en) * 1994-11-23 1996-03-19 Electronics & Telecommunications Research Institute Apparatus for adsorbing atomic hydrogen on surface
JP2006294608A (en) * 2005-04-06 2006-10-26 Samsung Sdi Co Ltd Method for manufacturing organic electroluminescent device
US8383208B2 (en) 2005-04-06 2013-02-26 Samsung Display Co., Ltd. Method of fabricating organic light emitting device

Also Published As

Publication number Publication date
JP2555209B2 (en) 1996-11-20

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