JPH01169920A - Continuous film forming device - Google Patents

Continuous film forming device

Info

Publication number
JPH01169920A
JPH01169920A JP62328509A JP32850987A JPH01169920A JP H01169920 A JPH01169920 A JP H01169920A JP 62328509 A JP62328509 A JP 62328509A JP 32850987 A JP32850987 A JP 32850987A JP H01169920 A JPH01169920 A JP H01169920A
Authority
JP
Japan
Prior art keywords
chamber
substrate
film forming
cleaning
reaction
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.)
Pending
Application number
JP62328509A
Other languages
Japanese (ja)
Inventor
Toshio Kawamura
河村 敏雄
Ryo Kimura
涼 木村
Yuko Toyonaga
豊永 由布子
Yasuhiko Tsukikawa
靖彦 月川
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP62328509A priority Critical patent/JPH01169920A/en
Publication of JPH01169920A publication Critical patent/JPH01169920A/en
Pending 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 prevent the dispersion of a film thickness and film quality by a method wherein a substrate in a reaction film forming chamber is rotated at the time of film formation and the flow velocity and the concentration distribution of reaction gas at each site on the substrate are made even. CONSTITUTION:The moment when a substrate stand 4 started to rotate by a rotary type heater, a reaction gas (a) is introduced and a film formation is generated. After the film formation, belts 6 are moved, a reaction film forming chamber 5 is carried out from a high-temperature chamber 7 and after the chamber 5 is cooled in the air, a substrate 3 is taken out and is carried in a cleaning chamber 12. The moment a cleaning substance introducing tube 13 and a cleaning substance discharge pipe 14, which are provided in the chamber 12, are combined with their respective introducing and discharge ports 1 and 2 in the chamber 5, the belts 6 are standstilled, a cleaning substance (c) is introduced and a cleaning is started. After the cleaning, the belts 6 are moved, the chamber 5 is carried out from the chamber 12 and a substrate 3 is installed anew and is carried in the chamber 7. Thereby, the variability of a film thickness and film quality is prevented.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、CVD反応を利用して薄膜形成を行う連続式
成膜装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a continuous film forming apparatus that forms a thin film using a CVD reaction.

従来の技術 近年、薄膜形成法として化学気相成長法(CVD法)は
その中核をなすものであり、非常に多く用いられるよう
になった。
BACKGROUND OF THE INVENTION In recent years, chemical vapor deposition (CVD) is the core of thin film forming methods and has come into widespread use.

CVD法は化学反応であるため、非常に広範囲かつ多様
な物質の薄膜形成が可能であり、また種々の気体反応材
料の組合せにより自由な組成の制御が可能となり、今ま
でに知られていなかったまたく新しい構造、組成の薄膜
を合成することもでき、しかもそれらの物質の融点より
も十分低い温度で形成することが可能となっている。
Since the CVD method is a chemical reaction, it is possible to form thin films of a very wide variety of substances, and by combining various gas-reactive materials, it is possible to freely control the composition. It is now possible to synthesize thin films with extremely new structures and compositions, and it is also possible to form them at temperatures well below the melting points of those materials.

最近、CVD法により薄膜形成の量産化が可能な連続式
成膜装置が開発されている。
Recently, a continuous film forming apparatus has been developed that is capable of mass-producing thin film formation using the CVD method.

以下図面を参照しながら、上述した従来の連続式成膜装
置の一例について説明する。
An example of the conventional continuous film forming apparatus mentioned above will be described below with reference to the drawings.

第3図は従来の連続式成膜装置の説明図である。FIG. 3 is an explanatory diagram of a conventional continuous film forming apparatus.

基板3を内部に設置した反応成膜室5がベルト6により
高温室7内部に搬入される。反応ガス導入による成膜後
、反応成膜室5は高温室7から搬出され、基板3取り一
出し後洗浄室12にて洗浄される。洗浄室12から搬出
された後、反応成膜室5は新しく基板3を設置し、高温
室7内へ搬入される。
A reaction film forming chamber 5 in which a substrate 3 is installed is carried into a high temperature chamber 7 by a belt 6. After film formation by introducing reactive gases, the reaction film forming chamber 5 is taken out from the high temperature chamber 7, and after the substrate 3 is taken out, it is cleaned in the cleaning chamber 12. After being carried out from the cleaning chamber 12, a new substrate 3 is installed in the reaction film forming chamber 5, and the substrate 3 is carried into the high temperature chamber 7.

以上の工程を複数の反応成膜室24を用いて連続的に行
う。
The above steps are performed continuously using a plurality of reaction film forming chambers 24.

発明が解決しようとする問題点 しかしながら上記のような構成では、反応成膜室内にお
いて反応ガスの流速、濃度分布が不均一なので膜厚、膜
質にばらつきが生じるという問題点を有していた。
Problems to be Solved by the Invention However, the above configuration has a problem in that the flow rate and concentration distribution of the reaction gas within the reaction film forming chamber are non-uniform, resulting in variations in film thickness and film quality.

本発明は上記問題点に鑑み、均一な膜厚、均一な膜質を
実現できる連続式成膜装置を提供するものである。
In view of the above problems, the present invention provides a continuous film forming apparatus that can realize uniform film thickness and uniform film quality.

問題点を解決するための手段 上記問題点を解決するために本発明の連続式成膜装置は
、成膜時において反応成膜室内の基板が回転するという
構造を備えたものである。
Means for Solving the Problems In order to solve the above problems, the continuous film forming apparatus of the present invention has a structure in which the substrate in the reaction film forming chamber rotates during film forming.

作用 本発明は上記した構成によって基板上の核部位における
反応ガスの流速と濃度分布が均一となるので、膜厚、膜
質にばらつきが生じない。
Effects In the present invention, the flow rate and concentration distribution of the reactant gas at the core site on the substrate are made uniform by the above-described configuration, so that variations in film thickness and film quality do not occur.

実施例 以下本発明の一実施例の連続式成膜装置について、図面
を参照しながら説明する。
EXAMPLE Hereinafter, a continuous film forming apparatus according to an example of the present invention will be described with reference to the drawings.

第1図は本発明の第1の実施例における連続式成膜装置
を示すものである。第1図において、導入口lと排出口
2を有し、その内部に基板3を載せた基板台4を設置し
た反応成膜室5がベルト6により高温室7内部に搬入さ
れる。尚、反応成膜室5には基板3出し入れのための気
密構造を有した開閉窓8が設けられている。また高温室
7は気体雰囲気を所定の温度に維持する空間を有してい
る。
FIG. 1 shows a continuous film forming apparatus according to a first embodiment of the present invention. In FIG. 1, a reaction film forming chamber 5 having an inlet 1 and an outlet 2 and in which a substrate table 4 on which a substrate 3 is placed is installed is carried into a high temperature chamber 7 by a belt 6. Incidentally, the reaction film forming chamber 5 is provided with an opening/closing window 8 having an airtight structure for taking the substrate 3 in and out. Further, the high temperature chamber 7 has a space for maintaining a gas atmosphere at a predetermined temperature.

高温室7内に設けられた反応ガス導入管9と排気ガス管
lOが反応成膜室5のそれぞれ導入口1、排出口2と合
体し、基板台4と回転式ヒーター11とが合体した瞬間
、ベルト6が静止する。基板3は回転式ヒーター11に
より成膜に必要な熱容量を受ける。
The moment when the reaction gas inlet pipe 9 and the exhaust gas pipe lO provided in the high temperature chamber 7 are combined with the inlet 1 and the exhaust port 2 of the reaction deposition chamber 5, respectively, and the substrate table 4 and the rotary heater 11 are combined. , the belt 6 comes to rest. The substrate 3 receives heat capacity necessary for film formation by a rotary heater 11.

基板台4が回転式ヒーター11により回転を始めた瞬間
、反応ガスaが導入され成膜が起こる。
The moment the substrate table 4 starts rotating by the rotary heater 11, the reaction gas a is introduced and film formation occurs.

高温室7内における成膜時には、反応ガスaと排気ガス
bが反応成膜室5外にもれない構造となっている。
During film formation in the high temperature chamber 7, the structure is such that the reaction gas a and the exhaust gas b do not leak out of the reaction film formation chamber 5.

成膜後ベルト6が動き、反応成膜室5は高温室7から搬
出され、大気中で冷却後基板3を取り出し、洗浄室12
に搬入される。
After film formation, the belt 6 moves, and the reaction film formation chamber 5 is carried out from the high temperature chamber 7, and after being cooled in the atmosphere, the substrate 3 is taken out and transferred to the cleaning chamber 12.
will be transported to.

洗浄室12に設けられた洗浄物質導入管13と洗浄物質
排出管14が、反応成膜室5のそれぞれ導入口1、排出
口2と合体した瞬間、ベルト6が静止し、洗浄物質Cが
導入され洗浄が開始される。
At the moment when the cleaning substance inlet pipe 13 and the cleaning substance discharge pipe 14 provided in the cleaning chamber 12 are combined with the inlet 1 and the outlet 2 of the reaction film forming chamber 5, respectively, the belt 6 comes to rest and the cleaning substance C is introduced. cleaning will begin.

洗浄室12内における洗浄時には、洗浄物質Cと排出物
dが反応成膜室5外にもれない構造となっている。
During cleaning in the cleaning chamber 12, the structure is such that the cleaning substance C and waste d do not leak out of the reaction film forming chamber 5.

洗浄後ベルト6が動き、反応成膜室5は洗浄室12から
搬出され、新しく基板3を設置し、高温室7内へ搬入さ
れる。
After cleaning, the belt 6 moves and the reaction film forming chamber 5 is carried out from the cleaning chamber 12, a new substrate 3 is installed, and the reaction film forming chamber 5 is carried into the high temperature chamber 7.

以上の工程を、複数の反応成膜室5を用いて連続的に行
う。
The above steps are performed continuously using a plurality of reaction film forming chambers 5.

このように構成された本装置での具体例として、アモル
ファスシリコン膜の形成について述べる。
As a specific example of this apparatus configured in this manner, the formation of an amorphous silicon film will be described.

導入口1と排出口2を水平方向に1つずつ有するステン
レス製反応成膜室5がベルト6により高温室7内部に搬
入された。反応成膜室5内には5×5cffiパイレツ
クス基板3を載せた基板台4が設置されており、高温室
7内は窒素(N2)雰囲気で760 Torrに維持さ
れ回転式ヒーター11により基板温度を460℃に保持
し、かつ垂直方向に10’C/備の温度勾配をもたせて
いる。
A stainless steel reaction film forming chamber 5 having one inlet 1 and one outlet 2 in the horizontal direction was carried into a high temperature chamber 7 by a belt 6. A substrate table 4 on which a 5×5 cffi Pyrex substrate 3 is mounted is installed in the reaction film forming chamber 5, and the temperature inside the high temperature chamber 7 is maintained at 760 Torr in a nitrogen (N2) atmosphere, and the substrate temperature is controlled by a rotary heater 11. The temperature was maintained at 460°C, and a temperature gradient of 10'C/unit was created in the vertical direction.

反応ガスとして水素(H2)で希釈された30%ジシラ
ン(S、i t H6) 150 SCCMを用い、基
板3を3Or、p、mで回転させ、5分間成膜を行った
。成膜後火気中で100℃になるまで冷却し、基板3を
取り出し、反応成膜室5は洗浄室12に搬入された。
Using 30% disilane (S, it H6) 150 SCCM diluted with hydrogen (H2) as a reaction gas, the substrate 3 was rotated at 3 Or, p, m, and film formation was performed for 5 minutes. After film formation, it was cooled to 100° C. in a flame, the substrate 3 was taken out, and the reaction film formation chamber 5 was transferred to the cleaning chamber 12.

洗浄物質として塩素CCl12)ガスを用い、5分間エ
ツチングした後反応成膜室5は洗浄室12がら検出され
、新しくパイレックス基板3を設置し、高温室7内へ搬
入された。
After etching for 5 minutes using chlorine (CCl12) gas as a cleaning substance, the reaction film forming chamber 5 was detected in the cleaning chamber 12, a new Pyrex substrate 3 was installed, and it was carried into the high temperature chamber 7.

こうして連続的に成膜した結果、基板3上に得られた膜
はすべてアモルファスシリコンであり、任意の10枚の
基板について各15部位の膜厚を測定すると4520人
±30人であった。さらにこれらの部位について分光測
定と電導度測定を行った結果、光学的エネルギーギャッ
プは1.6〜1.7eν、明導電率と暗導電率の比、す
なわち光感度は3〜5×104であった。尚、これらの
各部位の表面状態を表面検査ランプにより観察すること
によって、パーティクルを含まない光沢のある膜である
ということを確認した。
As a result of continuous film formation in this manner, all the films obtained on the substrate 3 were amorphous silicon, and the film thicknesses measured at each of 15 sites on arbitrary 10 substrates were 4520 ± 30. Furthermore, as a result of spectroscopic and conductivity measurements of these parts, the optical energy gap was 1.6 to 1.7 eν, and the ratio of bright conductivity to dark conductivity, that is, the photosensitivity, was 3 to 5 x 104. Ta. By observing the surface condition of each of these parts using a surface inspection lamp, it was confirmed that the film was shiny and did not contain particles.

以上のように本実施例によれば、反応成膜室5内での成
膜中に基板3を回転させることによって基板上の各部位
における反応ガスの流速と濃度分布が均一となるので、
膜厚、膜質のばらつきを防止することができる。
As described above, according to this embodiment, by rotating the substrate 3 during film formation in the reaction film formation chamber 5, the flow velocity and concentration distribution of the reaction gas at each location on the substrate become uniform.
Variations in film thickness and film quality can be prevented.

発明の効果 以上のように本発明は、成膜時において反応成膜室内の
基板が回転することにより、基板上の各部位における反
応ガスの流速と濃度分布が均一となるので、膜厚、膜質
のばらつきを防止することができ、大型かつ均質な薄膜
の量産装置として極めて有用である。
Effects of the Invention As described above, in the present invention, the rotation of the substrate in the reaction film formation chamber during film formation makes the flow rate and concentration distribution of the reaction gas uniform at each location on the substrate, resulting in improved film thickness and film quality. This method is extremely useful as a mass production device for large, homogeneous thin films.

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

第1図は本発明の一実施例の連続式成膜装置の斜視図、
第2図は本発明の一実施例の連続式成膜装置における成
膜中の高温室断面図、第3図は従来の連続式成膜装置の
斜視図である。 1・・・・・・導入口、2・・・・・・排出口、3・・
・・・・基板、4・・・・・・基板台、5・・・・・・
反応成膜室、6・・・・・・ベルト、7・・・・・・高
温室、8・・・・・・開閉窓、9・・・・・・反応ガス
導入管、10・・・・・・排気ガス管、11・・・・・
・回転式ヒーター、12・・・・・・洗浄室、13・・
・・・・洗浄物質導入管、14・・・・・・洗浄物質排
出管、21・・・・・・ヒーター。
FIG. 1 is a perspective view of a continuous film forming apparatus according to an embodiment of the present invention;
FIG. 2 is a sectional view of a high temperature chamber during film formation in a continuous film forming apparatus according to an embodiment of the present invention, and FIG. 3 is a perspective view of a conventional continuous film forming apparatus. 1...Inlet, 2...Outlet, 3...
... Board, 4... Board stand, 5...
Reaction film forming chamber, 6...Belt, 7...High temperature chamber, 8...Opening/closing window, 9...Reaction gas introduction pipe, 10... ...Exhaust gas pipe, 11...
・Rotary heater, 12...Cleaning room, 13...
...Cleaning substance inlet pipe, 14...Cleaning substance discharge pipe, 21...Heater.

Claims (3)

【特許請求の範囲】[Claims] (1)気体雰囲気を所定の温度に維持する空間を有する
高温室と、反応成膜室を洗浄する洗浄室とに分かれてお
り、個々に独立した反応成膜室を連続的に搬送し、成膜
時においては反応成膜室内の基板が回転することを特徴
とする連続式成膜装置。
(1) It is divided into a high-temperature chamber with a space for maintaining the gas atmosphere at a predetermined temperature and a cleaning chamber for cleaning the reaction film-forming chamber. A continuous film forming apparatus characterized in that the substrate inside the reaction film forming chamber rotates during film formation.
(2)基板の回転を反応成膜室内に設けた基板台を回転
させることにより行えることを特徴とする特許請求の範
囲第(1)項記載の連続式成膜装置。
(2) The continuous film forming apparatus according to claim (1), wherein the substrate can be rotated by rotating a substrate stand provided in the reaction film forming chamber.
(3)基板の回転が一方向若しくは交番であることを特
徴とする特許請求の範囲第(1)項記載の連続式成膜装
置。
(3) The continuous film forming apparatus according to claim (1), wherein the substrate is rotated in one direction or alternately.
JP62328509A 1987-12-24 1987-12-24 Continuous film forming device Pending JPH01169920A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62328509A JPH01169920A (en) 1987-12-24 1987-12-24 Continuous film forming device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62328509A JPH01169920A (en) 1987-12-24 1987-12-24 Continuous film forming device

Publications (1)

Publication Number Publication Date
JPH01169920A true JPH01169920A (en) 1989-07-05

Family

ID=18211068

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62328509A Pending JPH01169920A (en) 1987-12-24 1987-12-24 Continuous film forming device

Country Status (1)

Country Link
JP (1) JPH01169920A (en)

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