JP3108939B2 - Vapor phase growth method and apparatus - Google Patents

Vapor phase growth method and apparatus

Info

Publication number
JP3108939B2
JP3108939B2 JP03179634A JP17963491A JP3108939B2 JP 3108939 B2 JP3108939 B2 JP 3108939B2 JP 03179634 A JP03179634 A JP 03179634A JP 17963491 A JP17963491 A JP 17963491A JP 3108939 B2 JP3108939 B2 JP 3108939B2
Authority
JP
Japan
Prior art keywords
substrate
raw material
reaction tube
liquid
vapor phase
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 - Fee Related
Application number
JP03179634A
Other languages
Japanese (ja)
Other versions
JPH05175134A (en
Inventor
朝子 津山
浩 山崎
茂 林田
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.)
Taiyo Nippon Sanso Corp
Original Assignee
Taiyo Nippon Sanso Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Taiyo Nippon Sanso Corp filed Critical Taiyo Nippon Sanso Corp
Priority to JP03179634A priority Critical patent/JP3108939B2/en
Publication of JPH05175134A publication Critical patent/JPH05175134A/en
Application granted granted Critical
Publication of JP3108939B2 publication Critical patent/JP3108939B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、室温・常圧で固体もし
くは液体の原料を用いた気相成長方法及び装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vapor phase growth method and apparatus using a solid or liquid raw material at room temperature and normal pressure.

【0002】[0002]

【従来の技術】周知のように、気相成長方法は、反応管
内の所望の温度に加熱された基板上に原料ガスを供給し
て該基板上で熱分解させ、熱分解に伴って生ずる反応生
成物を前記基板上に堆積させて薄膜を形成するものであ
る。
2. Description of the Related Art As is well known, in a vapor phase growth method, a raw material gas is supplied to a substrate heated to a desired temperature in a reaction tube and is thermally decomposed on the substrate. The product is deposited on the substrate to form a thin film.

【0003】この場合、原料が室温・常圧で固体のとき
は、原料を所望の温度に加熱した原料容器内に収納する
とともに、該容器内に高温のキャリアガスを導入し、該
キャリアガスに原料の蒸気(原料ガス)を同伴させて反
応管内の前記基板上に供給し薄膜を形成する。
In this case, when the raw material is solid at room temperature and normal pressure, the raw material is stored in a raw material container heated to a desired temperature, a high-temperature carrier gas is introduced into the container, and the carrier gas is introduced into the container. The thin film is formed by supplying the raw material vapor (raw material gas) onto the substrate in the reaction tube together with it.

【0004】この際、基板上での薄膜の成長速度は、基
板上に供給される原料ガスの量が多いほど高まるので、
前記固体の原料を用いた気相成長では、前記原料容器ま
たはキャリアガスを高温にして原料の蒸気圧を高め、反
応管に供給する原料ガスの量を増加している。なお、原
料が液体の場合は、原料内にキャリアガスをバブリング
させることにより、前記同様にして基板上に原料の蒸気
(原料ガス)を供給している。
At this time, the growth rate of the thin film on the substrate increases as the amount of the source gas supplied to the substrate increases.
In the vapor phase growth using the solid raw material, the raw material container or the carrier gas is heated to a high temperature to increase the vapor pressure of the raw material, thereby increasing the amount of the raw material gas supplied to the reaction tube. When the raw material is a liquid, the raw material vapor (raw gas) is supplied to the substrate in the same manner as described above by bubbling a carrier gas into the raw material.

【0005】[0005]

【発明が解決しようとする課題】しかし、前記従来方法
では、原料容器または該容器に導入するキャリアガスの
温度を原料の分解温度以上に高めることはできない。こ
のため、基板上に供給できる原料ガスの最大量は、前記
分解温度に制約され、これ以上に薄膜の成長速度を高め
ることはできなかった。
However, in the conventional method, the temperature of the raw material container or the carrier gas introduced into the container cannot be increased to a temperature higher than the decomposition temperature of the raw material. For this reason, the maximum amount of the source gas that can be supplied onto the substrate is limited by the decomposition temperature, and the growth rate of the thin film cannot be further increased.

【0006】また、複数の原料を用いて基板上に薄膜を
製造する場合、複数の原料は比較的高温の原料ガスの状
態で混合されてキャリアガスに同伴されるため、各原料
ガスが反応してしまうことがある。この場合は、それぞ
れの原料ガスを、個々に反応管内に供給し、基板の近傍
で混合する必要があり、構造が複雑になる不都合があっ
た。
When a thin film is manufactured on a substrate by using a plurality of raw materials, the plurality of raw materials are mixed in a state of a relatively high-temperature raw material gas and accompanied by a carrier gas. Sometimes. In this case, each raw material gas must be individually supplied into the reaction tube and mixed near the substrate, which has a disadvantage that the structure becomes complicated.

【0007】[0007]

【課題を解決するための手段】本発明者等は、前記不都
合を解決すべく種々考究した結果、固体もしくは液体の
原料の蒸気をキャリアガスに同伴させるのではなく、原
料を液状にして反応管内に噴霧し、噴霧により得られる
霧状の原料を基板上に供給しても従来と同等の品質の薄
膜が得られ、かつ、従来より遥かに薄膜の成長速度を高
められることを知見した。
Means for Solving the Problems The present inventors have made various studies to solve the above-mentioned inconveniences. As a result, instead of entraining the vapor of a solid or liquid raw material with a carrier gas, the raw material is converted into a liquid state in the reaction tube. It has been found that a thin film having the same quality as that of the related art can be obtained even when the atomized raw material obtained by the spraying is supplied onto the substrate, and the growth rate of the thin film can be much higher than that of the related art.

【0008】本発明は、上記知見に基づいてなされたも
ので、本発明の気相成長方法は、液体原料を反応管内の
基板に向けて霧状に噴霧するとともに、噴霧された霧状
の液体原料の周囲から高温の不活性ガスを霧状の液体原
料に向けて噴射して液体原料を加熱気化して基板上に供
給し、該基板上で熱分解することを特徴としている。
[0008] The present invention has been made based on the above-mentioned findings .
Atomized spray toward the substrate
Of hot inert gas from around the liquid material
The liquid material is heated and vaporized by spraying
And thermally decompose on the substrate .

【0009】また、本発明の気相成長装置は、内部に基
板を配置する反応管と、該反応管内の基板を加熱する加
熱手段と、反応管の一端部に設けられて、前記基板に向
けて液体原料を霧状に噴霧する噴霧手段と、反応管内に
設置されて、内周面から霧状の液体原料に向けて高温の
不活性ガスを噴射するガス供給リングとを備えたことを
特徴としている
Further, the vapor phase growth apparatus of the present invention has an internal base.
A reaction tube in which a plate is placed and a substrate for heating the substrate in the reaction tube.
Heating means, provided at one end of the reaction tube, facing the substrate;
Spray means for spraying the liquid raw material in mist and
It is installed, and a high temperature
And a gas supply ring for injecting inert gas.
Features .

【0010】[0010]

【作 用】本発明によれば、液体原料は霧状、即ち微小
なエアロゾル状態で反応管内に噴霧され、噴霧された霧
状の液体原料は高温の不活性ガスによって加熱されてガ
ス化し、次いで熱分解して基板上に反応生成物が堆積し
薄膜が形成される。
According to the present invention, the liquid raw material is sprayed into the reaction tube in the form of a mist, that is, a fine aerosol, and the sprayed mist of the liquid raw material is heated by a high-temperature inert gas to be gasified. By thermal decomposition, a reaction product is deposited on the substrate to form a thin film.

【0011】なお、反応管内に噴霧するための液体原料
としては、原料自体が室温・常圧で粘度の低い液体の場
合はそのまま用いることができ、原料自体が室温・常圧
で固体の場合、または、粘度の高い液体の場合には有機
溶剤に溶解して用いることが望ましい。特に原料として
DPM(ジピバロイルメタン)系の原料を用いる場合に
は、有機溶剤としてTHF(テトラヒドロフラン),ト
リメチルアミン,DPM等を用いると、原料が重合し易
い場合に重合を抑え、原料が分解し易い場合に分解を抑
える作用があり、しかも形成される薄膜に悪影響を与え
ることがないので効果的である。
The liquid raw material to be sprayed into the reaction tube can be used as it is when the raw material itself is a liquid having low viscosity at room temperature and normal pressure, and when the raw material itself is solid at room temperature and normal pressure, Alternatively, in the case of a liquid having a high viscosity, it is desirable to dissolve it in an organic solvent before use. In particular, when a DPM (dipivaloylmethane) -based raw material is used as a raw material, when THF (tetrahydrofuran), trimethylamine, DPM, or the like is used as an organic solvent, polymerization is suppressed when the raw material is easily polymerized, and the raw material is decomposed. This is effective because it has the effect of suppressing decomposition when it is easy to perform, and does not adversely affect the formed thin film.

【0012】このように、本発明方法では液体原料を用
いるが、液体原料は予め所望の濃度に精密に調整でき、
また、噴霧量も精密に制御できるので、薄膜の品質とし
ては従来と同等にすることができる。
As described above, the liquid raw material is used in the method of the present invention, and the liquid raw material can be precisely adjusted to a desired concentration in advance.
Further, since the amount of spray can be precisely controlled, the quality of the thin film can be made equal to the conventional one.

【0013】そして特に、本発明方法は、原料を液状に
して反応管に導入するので、原料ガスをキャリアガスに
同伴させる従来方法に比べ、原料の濃度を遥かに高める
ことができ、多量の原料ガスを基板上に供給できるの
で、薄膜の成長速度を高め生産性を向上することができ
る。
In particular, in the method of the present invention, since the raw material is brought into a liquid state and introduced into the reaction tube, the concentration of the raw material can be significantly increased as compared with the conventional method in which the raw material gas is entrained in the carrier gas. Since the gas can be supplied onto the substrate, the growth rate of the thin film can be increased and the productivity can be improved.

【0014】[0014]

【実施例】以下、本発明を、図1に示す実施例に基づい
て、さらに詳細に説明する
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described based on an embodiment shown in FIG.
This will be described in further detail .

【0015】まず、図中、1は本装置を構成する反応管
である。反応管1の内部には、基板Pを保持するための
保持台2が設けられ、該保持台2に対応する位置の反応
管1の外周には、該保持台2を加熱するためのRFコイ
ル3が設けられている。これら保持台2及びRFコイル
3は、基板Pの加熱手段であり、基板PはRFコイル3
による保持台2の誘導加熱に伴う熱伝導により所望の温
度に設定される
First, in the figure, reference numeral 1 denotes a reaction tube constituting the present apparatus.
It is. The inside of the reaction tube 1 is for holding the substrate P.
A holding table 2 is provided, and a reaction at a position corresponding to the holding table 2 is performed.
An RF coil for heating the holding table 2 is provided on the outer circumference of the tube 1.
3 is provided. These holding table 2 and RF coil
3 is a heating means for the substrate P, and the substrate P is an RF coil 3
Desired temperature due to heat conduction accompanying induction heating of the holding table 2
Set to degree .

【0016】また、反応管1の一端部にはスプレーノズ
ル4(噴霧手段)が、他端部には排気管5が設けられ、
スプレーノズル4は、管6を介して液体原料を貯蔵する
容器(図示せず)の液相部に連通し、該容器の気相部に
は、適宜な加圧手段が管を介して連通している
A spray nozzle is provided at one end of the reaction tube 1.
The other end is provided with an exhaust pipe 5,
The spray nozzle 4 stores the liquid raw material via the pipe 6
Communicates with the liquid phase of a container (not shown),
Is connected to a suitable pressurizing means via a pipe .

【0017】上記構成において、基板PをRFコイル3
により所望の温度に加熱するとともに、管6を介して供
給される容器内の液体原料をスプレーノズル4から基板
Pに向けて霧状に噴霧する
In the above configuration, the substrate P is
To a desired temperature and supply via a pipe 6.
The liquid material in the container to be supplied is sprayed onto the
Spray toward P.

【0018】反応管1内には、同心二重のガス供給リン
グ12が設置されている。このガス供給リング12は、
スプレーノズル4から噴霧された霧状の液体原料が該リ
ング12の中央中空部を通過するよう構成するととも
に、該リング12の内周面12a全体から高温の不活性
ガスを反応管1の中心方向に向けて噴射するよう構成し
たものである
A concentric double gas supply phosphorus is provided in the reaction tube 1.
Group 12 is installed. This gas supply ring 12
The atomized liquid raw material sprayed from the spray nozzle 4 is
To pass through the central hollow part of the ring 12
In addition, the entire inner peripheral surface 12a of the ring 12 is inactive at a high temperature.
The gas is injected toward the center of the reaction tube 1.
It is a thing .

【0019】上記構成によれば、スプレーノズル4から
噴霧された霧状の液体原料の周囲から高温の不活性ガス
が霧状の液体原料に向けて噴射され、霧状の液体原料
は、リング12の中央中空部を通過する際に、高温の不
活性ガスにより加熱気化されるとともに、高温の不活性
ガスによって包まれ、霧状の原料が反応管1の内面に付
着して減少することなく基板Pに供給され、反応管1の
スプレーノズル4周辺を清浄に保持できるようにしたも
のである。また、これによって、液体原料は霧状になっ
て基板P上に供給され、該基板P上でガス化し、次いで
熱分解して反応生成物が基板P上に堆積し薄膜が形成さ
れる
According to the above configuration, from the spray nozzle 4
High temperature inert gas from around the atomized liquid raw material
Is sprayed toward the atomized liquid material, and the atomized liquid material
When passing through the central hollow portion of the ring 12,
Heated and vaporized by active gas, and inert at high temperature
A gaseous raw material wrapped in gas is attached to the inner surface of the reaction tube 1.
Is supplied to the substrate P without being reduced by
The area around the spray nozzle 4 can be kept clean.
It is. This also causes the liquid material to become a mist.
And supplied on the substrate P, gasified on the substrate P, and then
The thermal decomposition causes the reaction products to deposit on the substrate P to form a thin film.
It is .

【0020】[0020]

【発明の効果】以上のように、本発明によれば、液体原
料を霧状にして基板上に供給し、気相成長を行うので、
従来より遥かに多量の原料ガスを基板上に供給でき、薄
膜の成長速度を高めて生産性を向上することができる。
As described above, according to the present invention, the liquid source
Mist is supplied on the substrate in the form of a mist, and vapor phase growth is performed.
A much larger amount of source gas can be supplied onto the substrate
The productivity can be improved by increasing the growth rate of the film.

【0021】また、反応管内に噴霧された霧状の液体原Further, a mist-like liquid source sprayed into the reaction tube is used.
料は、高温の不活性ガスにより加熱気化されるとともThe material is heated and vaporized by hot inert gas and
に、高温の不活性ガスによって包まれ、霧状の原料が反, Which is wrapped in high-temperature inert gas,
応管の内面に付着して減少することなく基板Pに供給さIt is supplied to the substrate P without being reduced by adhering to the inner surface of the pipe.
れ、噴霧手段の周辺を清浄に保持できる。Thus, the periphery of the spraying means can be kept clean.

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

【図1】 本発明の一実施例を示す気相成長装置の系統
図である。
FIG. 1 is a system diagram of a vapor phase growth apparatus showing one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…反応管、2…保持台、3…RFコイル、4…スプレ
ーノズル、5…排気管、12…ガス供給リング、12a
…内周面、P…基板
DESCRIPTION OF SYMBOLS 1 ... Reaction tube, 2 ... Holder, 3 ... RF coil, 4 ... Spray nozzle, 5 ... Exhaust pipe, 12 ... Gas supply ring, 12a
… Inner surface, P… Substrate

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭50−147879(JP,A) 特開 昭61−244025(JP,A) 特開 平3−112894(JP,A) 特開 平3−8330(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01L 21/205 C23C 16/00 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-50-147879 (JP, A) JP-A-61-244025 (JP, A) JP-A-3-112894 (JP, A) JP-A-3-112894 8330 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) H01L 21/205 C23C 16/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 液体原料を反応管内の基板に向けて霧状
に噴霧するとともに、噴霧された霧状の液体原料の周囲
から高温の不活性ガスを霧状の液体原料に向けて噴射し
て液体原料を加熱気化して基板上に供給し、該基板上で
熱分解することを特徴とする気相成長方法。
1. A liquid material is atomized toward a substrate in a reaction tube.
Around the sprayed mist liquid material
Inject high-temperature inert gas toward the atomized liquid raw material from
To heat and vaporize the liquid raw material and supply it to the substrate,
A vapor phase growth method characterized by thermal decomposition .
【請求項2】 内部に基板を配置する反応管と、該反応
管内の基板を加熱する加熱手段と、反応管の一端部に設
けられて、前記基板に向けて液体原料を霧状に噴霧する
噴霧手段と、反応管内に設置されて、内周面から霧状の
液体原料に向けて高温の不活性ガスを噴射するガス供給
リングとを備えたことを特徴とする気相成長装置
2. A reaction tube in which a substrate is placed, and said reaction tube
Heating means for heating the substrate in the tube, and one end of the reaction tube
And sprays the liquid material in the form of a mist toward the substrate.
Spraying means, installed in the reaction tube, and atomized from the inner peripheral surface
Gas supply for injecting high-temperature inert gas toward liquid raw materials
A vapor phase growth apparatus comprising a ring .
JP03179634A 1991-07-19 1991-07-19 Vapor phase growth method and apparatus Expired - Fee Related JP3108939B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03179634A JP3108939B2 (en) 1991-07-19 1991-07-19 Vapor phase growth method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03179634A JP3108939B2 (en) 1991-07-19 1991-07-19 Vapor phase growth method and apparatus

Publications (2)

Publication Number Publication Date
JPH05175134A JPH05175134A (en) 1993-07-13
JP3108939B2 true JP3108939B2 (en) 2000-11-13

Family

ID=16069198

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03179634A Expired - Fee Related JP3108939B2 (en) 1991-07-19 1991-07-19 Vapor phase growth method and apparatus

Country Status (1)

Country Link
JP (1) JP3108939B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3595190B2 (en) 1999-04-16 2004-12-02 株式会社日立製作所 Semiconductor manufacturing method and semiconductor manufacturing apparatus
JP2001308082A (en) 2000-04-20 2001-11-02 Nec Corp Method of vaporizing liquid organic material and method of growing insulation film
JP2006070342A (en) * 2004-09-03 2006-03-16 Sumitomo Electric Ind Ltd Vapor phase film deposition system, susceptor and vapor phase film deposition method
JP6342370B2 (en) 2015-09-07 2018-06-13 株式会社東芝 Semiconductor manufacturing apparatus and removal apparatus for semiconductor manufacturing apparatus

Also Published As

Publication number Publication date
JPH05175134A (en) 1993-07-13

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