JPH06232048A - Device for vaporizing and supplying organometallic compound - Google Patents

Device for vaporizing and supplying organometallic compound

Info

Publication number
JPH06232048A
JPH06232048A JP1393893A JP1393893A JPH06232048A JP H06232048 A JPH06232048 A JP H06232048A JP 1393893 A JP1393893 A JP 1393893A JP 1393893 A JP1393893 A JP 1393893A JP H06232048 A JPH06232048 A JP H06232048A
Authority
JP
Japan
Prior art keywords
organometallic compound
vaporization
container
powder
carrier gas
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
JP1393893A
Other languages
Japanese (ja)
Inventor
Atsushi Tomosawa
淳 友澤
Masuzo Hattori
益三 服部
Hideo Torii
秀雄 鳥井
Akiyuki Fujii
映志 藤井
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 JP1393893A priority Critical patent/JPH06232048A/en
Publication of JPH06232048A publication Critical patent/JPH06232048A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To maintain a vaporizing container at a vaporizing temperature containing less errors as a whole by arranging a saucer to be filled with the powder of an organometallic compound in the container and forming carrier gas flowing-in and flowing-out holes through the side wall of the container. CONSTITUTION:A vaporizing container 11 is dipped in oil 9 contained in an oil bath 8 constituting a constant-temperature bath. The flowing-out hole 12 of a carrier gas 14 and starting gaseous material to a CVD reaction device 15 and the flowing-in hole of the carrier gas 14 to container 11 are interposed to each other. The saucer 16 to be filled with an organometallic compound 4 which is used as the raw material has such a shape that the surface area of the saucer 16 does not change even when the amount of the compound 4 decreases by evaporation. The holes 10 and 12 are formed through the side wall of the container 11 at heights higher than the saucer 16 and interposed to each other. Therefore, thin films which always have the same characteristic values under the same condition can be obtained.

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、有機金属化合物を原料
とする気相成長法(MO−CVD法)により、化合物半導
体,誘電体,超伝導体,磁性体等の薄膜を製造する場合
に、その原料として用いられる固体原料の有機金属化合
物の気化供給装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is applied to the production of thin films of compound semiconductors, dielectrics, superconductors, magnetic materials, etc. by a vapor phase growth method (MO-CVD method) using an organometallic compound as a raw material. The present invention relates to an apparatus for vaporizing and supplying an organometallic compound which is a solid raw material used as the raw material.

【0002】[0002]

【従来の技術】近年の電子機器の小型化,軽量化,高性
能化にともない、磁性材料や誘電体材料などを薄膜化す
る試みが数多くなされており、様々な成膜方法が研究さ
れている。その成膜方法の一つである原料に有機金属化
合物を用いたMO−CVD法は、比較的低い真空度のも
とで、大面積の薄膜を高速で得ることができるため、産
業的に優れた成膜方法である。
2. Description of the Related Art With the recent miniaturization, weight reduction and high performance of electronic devices, many attempts have been made to thin magnetic materials and dielectric materials, and various film forming methods have been studied. . The MO-CVD method using an organometallic compound as a raw material, which is one of the film forming methods, is industrially excellent because a large-area thin film can be obtained at a high speed under a relatively low degree of vacuum. Another film forming method.

【0003】MO−CVD法において、原料である固体
の有機金属化合物を気化させてCVD反応装置に導入す
る方法としては、従来から石英ボート上に固体原料の有
機金属化合物の粉末を入れ、これを減圧下の石英管内に
置き、石英管外部より電気抵抗ヒーターにより加熱して
気化させ、流量を制御したキャリアガスとともに導入す
るという方法が一般的であった。
In the MO-CVD method, as a method of vaporizing a solid organometallic compound which is a raw material and introducing it into a CVD reactor, a powder of a solid organometallic compound which is a solid raw material has been conventionally put in a quartz boat. It is a general method to place in a quartz tube under reduced pressure, vaporize by heating with an electric resistance heater from the outside of the quartz tube, and introduce with a carrier gas whose flow rate is controlled.

【0004】図2はこの方法による従来の気化供給装置
の構成図を示す。同図において、1はキャリアガス14の
流量を制御するマスフローコントローラー(MFC),2
は石英管、3は石英ボート、4は原料の有機金属化合
物、5は熱電対、6は電気抵抗ヒーター、7は気化温度
を制御する温度コントローラーである。
FIG. 2 is a block diagram of a conventional vaporizing and supplying apparatus according to this method. In the figure, 1 is a mass flow controller (MFC) for controlling the flow rate of the carrier gas 14, 2
Is a quartz tube, 3 is a quartz boat, 4 is a raw material organometallic compound, 5 is a thermocouple, 6 is an electric resistance heater, and 7 is a temperature controller for controlling the vaporization temperature.

【0005】この装置は以下のように使用する。まず原
料の有機金属化合物4を所定量、石英ボート3上に入れ
る。これを石英管2内に入れ、真空ポンプにより減圧す
る。石英管2と、その中の石英ボート3全体を電気抵抗
ヒーター6により加熱し、熱電対5と温度コントローラ
ー7により所定の温度に保ち、原料の有機金属化合物4
を気化させる。そこにマスフローコントローラー1によ
って流量を制御されたキャリアガス14を石英管2内に流
し、気化した原料ガスとともにCVD反応装置15に導入
する。このようなCVD反応装置の気化供給装置につい
ては、例えばジャーナル・オブ・マテリアル・サイエン
ス(1989年)第3549頁から第3552頁に発表されている。
This device is used as follows. First, a predetermined amount of the organometallic compound 4 as a raw material is put on the quartz boat 3. This is put in the quartz tube 2 and decompressed by a vacuum pump. The quartz tube 2 and the entire quartz boat 3 in the quartz tube 2 are heated by an electric resistance heater 6 and kept at a predetermined temperature by a thermocouple 5 and a temperature controller 7.
Vaporize. A carrier gas 14 whose flow rate is controlled by the mass flow controller 1 is flown into the quartz tube 2 and introduced into the CVD reactor 15 together with the vaporized source gas. Such a vaporization supply device for a CVD reactor is disclosed, for example, in Journal of Material Science (1989), pages 3549 to 3552.

【0006】しかし、このような気化供給装置を作製し
て成膜を行なった場合、同じ条件で原料を気化し成膜し
ても、膜厚や各種の物性値がばらつくという問題があっ
た。この原因は、有機金属化合物4の加熱に石英管2の
外側に位置する電気抵抗ヒーター6を使うために、原料
気化温度にばらつきが生じることや、石英ボート3上の
原料が徐々に減少していくためにキャリアガス14に触れ
る面積が変わり、原料の気化量が変わってしまうことに
あると考えられる。
However, in the case where such a vaporization supply device is manufactured and film formation is performed, there is a problem that the film thickness and various physical property values vary even if the raw material is vaporized and formed under the same conditions. This is because the electric resistance heater 6 located outside the quartz tube 2 is used to heat the organometallic compound 4, so that the vaporization temperature of the raw material varies and the raw material on the quartz boat 3 gradually decreases. It is conceivable that the area in contact with the carrier gas 14 changes as the process proceeds and the amount of vaporization of the raw material changes.

【0007】そこで、この課題を解決するため、円柱型
の気化容器に、直接、有機金属化合物の粉末を充填し、
この気化容器をオイルバス中に沈めて加熱し、上方より
流量を制御したキャリアガスを流し、再び上方より原料
ガスとともにCVD反応装置に導入するという気化供給
装置が提案されている。
In order to solve this problem, therefore, a cylindrical vaporization container is directly filled with powder of an organometallic compound,
A vaporization supply device has been proposed in which this vaporization container is immersed in an oil bath for heating, a carrier gas whose flow rate is controlled is made to flow from above, and is introduced into the CVD reaction device together with the source gas from above again.

【0008】図3はこの方法による気化供給装置の構成
図を示す。同図において、8はオイルバス、9はオイ
ル、10はキャリアガス14の流入孔、11は気化容器、12は
キャリアガス14と原料ガスの流出孔、13は気化容器11の
蓋である。その他、図2と同じ部材には同じ符号を付
し、その説明を省略する。
FIG. 3 is a block diagram of a vaporization and supply device according to this method. In the figure, 8 is an oil bath, 9 is oil, 10 is an inlet for carrier gas 14, 11 is a vaporization container, 12 is an outlet for carrier gas 14 and source gas, and 13 is a lid for the vaporization container 11. In addition, the same members as those in FIG. 2 are denoted by the same reference numerals, and the description thereof will be omitted.

【0009】この装置は、以下のように使用する。まず
原料の有機金属化合物4を気化容器11内に充填する。流
入孔10と流出孔12の付いた蓋13を気化容器11に取り付
け、オイルバス8のオイル9中に沈める。気化容器11
を、オイルバス8によりオイル9を介して加熱し、気化
容器11の直下に設置した熱電対5と温度コントローラー
7により所定の温度に保つ。マスフローコントローラー
1により流量を制御されたキャリアガス14を流入孔10よ
り気化容器11内に流し、気化した原料ガスとともに流出
孔12よりCVD反応装置15に導入する。このようなCV
D反応装置の気化供給装置については、例えば日本応用
磁気学会誌(1988年)第339頁から342頁に発表されてい
る。
This device is used as follows. First, the raw material organometallic compound 4 is filled in the vaporization container 11. A lid 13 having an inflow hole 10 and an outflow hole 12 is attached to the vaporization container 11 and submerged in the oil 9 in the oil bath 8. Vaporization container 11
Is heated by an oil bath 8 via oil 9, and is kept at a predetermined temperature by a thermocouple 5 and a temperature controller 7 installed immediately below the vaporization container 11. A carrier gas 14 whose flow rate is controlled by the mass flow controller 1 is caused to flow into the vaporization container 11 through the inflow hole 10 and is introduced into the CVD reaction device 15 through the outflow hole 12 together with the vaporized raw material gas. CV like this
The vaporization supply device of the D reactor is disclosed in, for example, Journal of Applied Magnetics of Japan (1988), pages 339 to 342.

【0010】[0010]

【発明が解決しようとする課題】しかし、前記図3に示
すような気化供給装置を用いて成膜を行なった場合、同
じ条件で原料を気化し成膜しても、やはり膜厚や各種の
物性値が若干ばらつくという問題があった。この原因
は、気化した有機金属化合物4の原料ガスをCVD反応
装置15に供給するキャリアガス14が、気化容器の上方の
流入孔10より流入し、原料ガスとともに再び上方の流出
孔12より流出するため、気化容器11内のガスの流れに乱
れが生じ、気化した原料ガスを全てCVD反応装置15に
供給することができないことや、有機金属化合物の加熱
に、オイルバス8を用いて加熱を行なうことにより、非
常に誤差の少ない気化温度が設定できるが、気化容器11
の上部が大気中にあるため、気化容器内に温度勾配が生
じてしまうことが、原料ガスの安定供給を妨げているこ
とにあると考えられる。
However, when a film is formed by using the vaporization supply device as shown in FIG. 3, even if the raw material is vaporized under the same conditions to form the film, the film thickness and various types of film are still generated. There was a problem that the physical property values were slightly different. The reason for this is that the carrier gas 14 for supplying the vaporized source gas of the organometallic compound 4 to the CVD reactor 15 flows in through the inflow hole 10 above the vaporization vessel, and flows out again through the outflow hole 12 together with the source gas. Therefore, turbulence occurs in the gas flow in the vaporization container 11, and it is not possible to supply all of the vaporized raw material gas to the CVD reactor 15. Also, the heating of the organometallic compound is performed using the oil bath 8. By doing so, the vaporization temperature with very few errors can be set.
It is considered that the temperature gradient in the vaporization container hinders the stable supply of the raw material gas because the upper part of the is in the atmosphere.

【0011】本発明はこのような従来の問題点を解決
し、常に同じ条件で同じ特性値をもつ薄膜を得ることが
できる有機金属化合物の気化供給装置の提供を目的とす
る。
An object of the present invention is to solve the above-mentioned conventional problems and to provide a vaporization and supply device of an organometallic compound which can always obtain a thin film having the same characteristic value under the same conditions.

【0012】[0012]

【課題を解決するための手段】本発明の有機金属化合物
の気化供給装置は、気化容器と、該気化容器を入れる恒
温槽を有し、前記気化容器はその内部に有機金属化合物
の粉末を充填する皿が配置され、前記気化容器の側壁に
キャリアガスの流入孔および流出孔が配置されているこ
とを特徴とする。
The apparatus for vaporizing and supplying an organometallic compound according to the present invention has a vaporization container and a constant temperature bath for containing the vaporization container, and the vaporization container is filled with the powder of the organometallic compound. And a carrier gas inflow hole and a carrier gas outflow hole are arranged in the side wall of the vaporization container.

【0013】前記有機金属化合物の気化供給装置におけ
るキャリアガスの流入孔と流出孔が、気化容器内に配置
した有機金属化合物の粉末を充填する皿より上方の側壁
に位置し、それぞれが向い合わせに配置されることによ
り、キャリアガスが有機金属化合物の粉末の表面と平行
に流れるように構成される。
The carrier gas inflow hole and outflow hole in the vaporizing and supplying apparatus for the organometallic compound are located on the side wall above the dish filled with the organometallic compound powder placed in the vaporizing vessel, and face each other. By being arranged, the carrier gas is configured to flow parallel to the surface of the powder of the organometallic compound.

【0014】また、前記気化容器内の有機金属化合物の
粉末を充填する皿は、その内部に充填した有機金属化合
物の粉末の表面の面積が、当該有機金属化合物の粉末の
気化による減少に関わらず、常に一定であるような形状
を有する。
Further, in the dish filled with the powder of the organometallic compound in the vaporization container, the surface area of the surface of the powder of the organometallic compound filled in the dish is not affected by the vaporization of the powder of the organometallic compound. , Having a shape that is always constant.

【0015】さらに、前記恒温槽がオイルバスで構成さ
れ、気化容器全体をオイルバス中に沈め、オイルの温度
を制御して気化容器全体を加熱することにより、有機金
属化合物の粉末の気化温度を制御するようになってい
る。
Further, the constant temperature bath is composed of an oil bath, and the vaporization temperature of the powder of the organometallic compound is controlled by submerging the entire vaporization vessel in the oil bath and controlling the temperature of the oil to heat the entire vaporization vessel. It is designed to be controlled.

【0016】[0016]

【作用】本発明によれば、原料の有機金属化合物の粉末
を、その表面の面積が原料の気化による減少に関わら
ず、常に一定であるような形状の皿に充填し、この皿を
入れた気化容器内に、キャリアガスを、有機金属化合物
の粉末の表面と平行に流して原料ガスをCVD反応装置
に供給することにより、常に安定した原料ガス供給量を
保つことができる。さらに原料の有機金属化合物の加熱
に、気化容器全体を恒温槽(例えばオイルバス)中に入れ
ることにより、気化容器全体を非常に誤差の少ない気化
温度に保つことができる有機金属化合物の気化供給装置
を提供するものである。
According to the present invention, the powder of the organometallic compound as a raw material is filled in a dish whose surface area is always constant regardless of the decrease in the surface area due to the vaporization of the raw material, and the dish is placed. By supplying the source gas to the CVD reactor by flowing the carrier gas in the vaporization container in parallel with the surface of the powder of the organometallic compound, it is possible to always maintain a stable supply amount of the source gas. Furthermore, for heating the organometallic compound as a raw material, by putting the entire vaporization container in a thermostatic bath (for example, an oil bath), the vaporization supply device for the organometallic compound that can maintain the vaporization temperature of the entire vaporization container with very few errors Is provided.

【0017】したがって、本発明の有機金属化合物の気
化供給装置を用いれば、常に同じ気化条件で、同じ特性
値を持った薄膜を得ることができる。また、原料の有機
金属化合物を充填する皿が別になっているため、原料の
入れ替えや、気化容器内の清掃が容易であるといった利
点も持っている。
Therefore, by using the apparatus for vaporizing and supplying an organometallic compound of the present invention, it is possible to obtain a thin film having the same characteristic values under the same vaporization conditions. In addition, since the plate for filling the organometallic compound as a raw material is separately provided, it has an advantage that it is easy to replace the raw material and clean the inside of the vaporization container.

【0018】[0018]

【実施例】以下、本発明の一実施例の有機金属化合物気
化供給装置について、図面を参照しながら説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An organometallic compound vaporizing and supplying apparatus according to an embodiment of the present invention will be described below with reference to the drawings.

【0019】図1は本発明の一実施例における有機金属
化合物の気化供給装置の構成図を示すものである。
FIG. 1 is a block diagram of an apparatus for vaporizing and supplying an organometallic compound according to an embodiment of the present invention.

【0020】本実施例の構成の特徴は、図1に示すよう
に、恒温槽はオイルバス8で構成され、このオイルバス
8内のオイル9中に気化容器11は配置される。CVD反
応装置15へのキャリアガス14および原料ガスの流出孔12
と、キャリアガス14の流入孔10とはそれぞれ向い合わせ
に位置する。また原料の有機金属化合物4を充填する皿
16は、その中に充填された原料の有機金属化合物4が、
気化することによって減少しても、表面の面積が変わら
ないような形状を有している。そして、前記流入孔10と
流出孔12は、気化容器11内に配置した有機金属化合物4
の粉末を充填する皿16より上方の側壁に位置し、それぞ
れ向い合わせになっている。その他、前記図3と同じ部
材には同じ番号を付してある。
As shown in FIG. 1, the constitution of this embodiment is characterized in that the constant temperature bath is constituted by an oil bath 8, and a vaporization container 11 is arranged in the oil 9 in the oil bath 8. Outflow hole 12 for carrier gas 14 and source gas to CVD reactor 15
And the inflow holes 10 for the carrier gas 14 are positioned to face each other. Also, a dish filled with the organometallic compound 4 as a raw material
16 is the organic metal compound 4 of the raw material filled in
It has such a shape that the surface area does not change even if it is reduced by vaporization. The inflow hole 10 and the outflow hole 12 are formed of the organometallic compound 4 arranged in the vaporization vessel 11.
Are located on the side wall above the dish 16 for filling the powder, and face each other. In addition, the same members as those in FIG. 3 are designated by the same reference numerals.

【0021】次に使用方法を説明すると、皿16を気化容
器11の中に入れ、密閉した後、気化容器11全体をオイル
バス8のオイル9中に沈める。気化容器11をオイルバス
8よりオイル9を介して加熱し、気化容器11の直下に設
置した熱電対5と、温度コントローラー7により所定の
気化温度に保つ。マスフローコントローラー1により流
量を制御されたキャリアガス14を、流入孔10より気化容
器11内に流し、気化した原料ガスとともに流出孔12より
CVD反応装置15に導入する。この場合のキャリアガス
は有機金属化合物の粉末の表面と平行に流れるので、原
料ガスがCVD反応装置に供給されることにより、常に
安定した原料ガスの供給量を保つことができる。
To explain the method of use, the dish 16 is placed in the vaporization container 11 and sealed, and then the entire vaporization container 11 is submerged in the oil 9 in the oil bath 8. The vaporization container 11 is heated from the oil bath 8 through the oil 9, and is kept at a predetermined vaporization temperature by the thermocouple 5 installed immediately below the vaporization container 11 and the temperature controller 7. A carrier gas 14 whose flow rate is controlled by the mass flow controller 1 is caused to flow into the vaporization vessel 11 through the inflow hole 10 and is introduced into the CVD reaction device 15 through the outflow hole 12 together with the vaporized source gas. In this case, the carrier gas flows in parallel with the surface of the powder of the organometallic compound, so that by supplying the raw material gas to the CVD reactor, it is possible to always maintain a stable supply amount of the raw material gas.

【0022】なお、本実施例の気化容器のキャリアガス
の流入孔および流出孔は、それぞれ1つずつであった
が、これらが複数の場合でも、ガスの流れが乱れない位
置にある限り、同様の効果が得られるのは言うまでもな
い。
The vaporization container of this embodiment has one carrier gas inflow hole and one carrier gas outflow hole. However, even if a plurality of carrier gas inflow holes and outflow holes are provided, they are the same as long as the gas flow is not disturbed. Needless to say, the effect of can be obtained.

【0023】[0023]

【発明の効果】以上説明したように、本発明の有機金属
化合物の気化供給装置は、原料の有機金属化合物を、そ
の表面の面積が原料の気化による減少に関わらず、常に
一定であるような形状の皿に充填し、この皿を入れた気
化容器内に、キャリアガスを、有機金属化合物の粉末の
表面と平行に流すことにより、常に安定した気化量を保
つことができる。さらに原料の有機金属化合物の加熱
に、気化容器全体をオイルバス中に沈め、温度変化の少
ないオイルを介して加熱することにより、気化容器全体
を非常に安定した誤差の少ない気化温度(温度誤差は±
0.5℃以内)に保つことができる。そのため、ガスの流れ
の乱れや温度勾配によって起きる気化量の変化がなく、
常に同じ条件で同じ特性値を持った薄膜を得ることがで
きる実用上極めて有利なものである。
As described above, the apparatus for vaporizing and supplying an organometallic compound according to the present invention is such that the surface area of the organometallic compound as a raw material is always constant regardless of the decrease due to the vaporization of the raw material. It is possible to always maintain a stable vaporization amount by filling a shaped dish and flowing the carrier gas in the vaporization vessel containing the dish in parallel with the surface of the powder of the organometallic compound. In addition, when heating the organometallic compound as a raw material, the entire evaporation container is submerged in an oil bath and heated through oil whose temperature changes little, so that the entire evaporation container is extremely stable and has a low evaporation temperature (temperature error is ±
Can be kept within 0.5 ° C). Therefore, there is no change in vaporization amount caused by turbulence of gas flow or temperature gradient,
It is extremely advantageous in practice that a thin film having the same characteristic values can always be obtained under the same conditions.

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

【図1】本発明の一実施例の有機金属化合物の気化供給
装置の構成図である。
FIG. 1 is a configuration diagram of a vaporization and supply device for an organometallic compound according to an embodiment of the present invention.

【図2】従来の有機金属化合物の気化供給装置の構成図
である。
FIG. 2 is a configuration diagram of a conventional vaporization and supply device of an organometallic compound.

【図3】従来の別の有機金属化合物の気化供給装置の構
成図である。
FIG. 3 is a configuration diagram of another conventional vaporizing and supplying device of an organometallic compound.

【符号の説明】[Explanation of symbols]

1…マスルトーコントローラー、 4…有機金属化合
物、 5…熱電対、 7…温度コントローラー、 8…
オイルバス、 9…オイル、 10…流入孔、 11…気化
容器、 12…流出孔、 13…蓋、 14…キャリアガス、
15…CVD反応装置、 16…皿。
1 ... masuto controller, 4 ... organometallic compound, 5 ... thermocouple, 7 ... temperature controller, 8 ...
Oil bath, 9 ... Oil, 10 ... Inflow port, 11 ... Vaporization container, 12 ... Outflow port, 13 ... Lid, 14 ... Carrier gas,
15 ... CVD reactor, 16 ... dish.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 藤井 映志 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Eiji Fujii 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 有機金属化合物化学蒸着成膜装置に用い
るCVD原料ガスを供給するための有機金属化合物固体
原料の気化供給装置における気化容器と、前記気化容器
を入れる恒温槽を有し、前記気化容器はその内部に有機
金属化合物の粉末を充填する皿が配置され、前記気化容
器の側壁にキャリアガスの流入孔および流出孔が配置さ
れていることを特徴とする有機金属化合物の気化供給装
置。
1. A vaporization container in a vaporization supply device of a metalorganic compound solid raw material for supplying a CVD raw material gas used in a metalorganic chemical vapor deposition apparatus, and a constant temperature bath for accommodating the vaporization container, comprising: A vaporization supply device for an organometallic compound, characterized in that a vessel for filling powder of the organometallic compound is arranged inside the vessel, and an inlet hole and an outlet hole for a carrier gas are arranged on a side wall of the vaporization vessel.
【請求項2】 前記キャリアガスの流入孔と流出孔が、
気化容器内に配置した有機金属化合物の粉末を充填する
皿より上方の側壁に位置し、それぞれが向い合わせに配
置されることにより、キャリアガスが有機金属化合物の
粉末の表面と平行に流れることを特徴とする請求項1記
載の有機金属化合物の気化供給装置。
2. The carrier gas inflow hole and outflow hole
Located on the side wall above the dish filled with the powder of the organometallic compound placed in the vaporization vessel, and by arranging them facing each other, the carrier gas can flow in parallel with the surface of the powder of the organometallic compound. The apparatus for vaporizing and supplying an organometallic compound according to claim 1.
【請求項3】 前記気化容器内の有機金属化合物の粉末
を充填する皿は、その内部に充填した有機金属化合物の
粉末の表面の面積が、当該有機金属化合物の粉末の気化
による減少に関わらず、常に一定であるような形状を有
することを特徴とする請求項1記載の有機金属化合物の
気化供給装置。
3. The plate filled with the powder of the organometallic compound in the vaporization container has a surface area of the powder of the organometallic compound filled therein which is reduced by vaporization of the powder of the organometallic compound. The apparatus for vaporizing and supplying an organometallic compound according to claim 1, having a shape which is always constant.
【請求項4】 前記恒温槽がオイルバスで構成され、気
化容器全体をオイルバス中に沈め、オイルの温度を制御
して気化容器全体を加熱することにより、有機金属化合
物の粉末の気化温度を制御することを特徴とする請求項
1記載の有機金属化合物の気化供給装置。
4. The vaporization temperature of the powder of the organometallic compound is controlled by heating the vaporization vessel by controlling the temperature of the oil by submerging the entire vaporization vessel in the oil bath as the constant temperature bath. It controls, The vaporization supply apparatus of the organometallic compound of Claim 1 characterized by the above-mentioned.
JP1393893A 1993-01-29 1993-01-29 Device for vaporizing and supplying organometallic compound Pending JPH06232048A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1393893A JPH06232048A (en) 1993-01-29 1993-01-29 Device for vaporizing and supplying organometallic compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1393893A JPH06232048A (en) 1993-01-29 1993-01-29 Device for vaporizing and supplying organometallic compound

Publications (1)

Publication Number Publication Date
JPH06232048A true JPH06232048A (en) 1994-08-19

Family

ID=11847149

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1393893A Pending JPH06232048A (en) 1993-01-29 1993-01-29 Device for vaporizing and supplying organometallic compound

Country Status (1)

Country Link
JP (1) JPH06232048A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07321040A (en) * 1994-05-24 1995-12-08 Nec Corp Metallic compound container
WO2007072867A1 (en) * 2005-12-22 2007-06-28 Tokyo Electron Limited Feedstock supply unit and vapor deposition equipment
KR101536717B1 (en) * 2014-07-18 2015-07-15 (주)스마트코리아 Nonvacuum buffer layer deposition apparatus of CIGS Solar Cell

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07321040A (en) * 1994-05-24 1995-12-08 Nec Corp Metallic compound container
WO2007072867A1 (en) * 2005-12-22 2007-06-28 Tokyo Electron Limited Feedstock supply unit and vapor deposition equipment
JP2007169728A (en) * 2005-12-22 2007-07-05 Tokyo Electron Ltd Raw material feeder, and vapor deposition apparatus
KR100981474B1 (en) * 2005-12-22 2010-09-10 도쿄엘렉트론가부시키가이샤 Feedstock supply unit and vapor deposition equipment
KR101536717B1 (en) * 2014-07-18 2015-07-15 (주)스마트코리아 Nonvacuum buffer layer deposition apparatus of CIGS Solar Cell

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