JP2003273093A - Feeding method of solid organic metal, and its feeder - Google Patents

Feeding method of solid organic metal, and its feeder

Info

Publication number
JP2003273093A
JP2003273093A JP2002066953A JP2002066953A JP2003273093A JP 2003273093 A JP2003273093 A JP 2003273093A JP 2002066953 A JP2002066953 A JP 2002066953A JP 2002066953 A JP2002066953 A JP 2002066953A JP 2003273093 A JP2003273093 A JP 2003273093A
Authority
JP
Japan
Prior art keywords
organic metal
raw material
carrier
solid
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
JP2002066953A
Other languages
Japanese (ja)
Inventor
Kozo Toyama
綱造 外山
Ayanori Endo
文徳 遠藤
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.)
Canon Inc
Original Assignee
Canon Inc
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 Canon Inc filed Critical Canon Inc
Priority to JP2002066953A priority Critical patent/JP2003273093A/en
Publication of JP2003273093A publication Critical patent/JP2003273093A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/448Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials
    • C23C16/4481Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials by evaporation using carrier gas in contact with the source material

Abstract

<P>PROBLEM TO BE SOLVED: To provide a feeding method of a solid organic metal or the like for efficiently and stably feeding a concentrated source gas for a long time. <P>SOLUTION: The solid organic metal 3, carried on a surface having a large number of through-holes (not shown), penetrating from one end face of an organic metal carrier 1 carrying the solid organic metal 3 to the other end face, is held in an atmosphere of a temperature in which the solid organic metal 3 undergoes sublimation. The source gas obtained by mixing the solid organic metal 3 is fed to carrier gas, by passing the carrier gas through each through-hole. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、固体有機金属を原
料として有機金属気相成長(MOCVD)法により薄膜
を形成する成膜装置に固体有機金属を供給する、固体有
機金属の供給方法及びその供給装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for supplying a solid organic metal to a film forming apparatus for forming a thin film from the solid organic metal as a raw material by a metal organic chemical vapor deposition (MOCVD) method, and a method for supplying the same. Regarding the feeding device.

【0002】[0002]

【従来の技術】従来から、強誘電体の酸化物薄膜や化合
物半導体薄膜などの作製方法として、スパッタ法、レー
ザーアブレーション(PLD)法、分子線エピタキシャ
ル(MBE)法、有機金属気相成長(MOCVD)法、
ゾルーゲル法などが試みられている。中でもMOCVD
法は、優れた段差被覆性を有し、大面積への成膜が可能
であり、比較的低温で成膜できるといった特徴を持つた
め、薄膜の成長を効率よく、容易に行うことができる。
酸化物薄膜を形成する場合、MOCVDの原料として
は、例えば150℃〜200℃の温度で昇華による蒸気
圧が比較的高くとれるジピバロイルメタン(DPM)金
属錯体等が用いられる。強誘電体酸化物であるチタン酸
ジルコン酸鉛(PZT)の有機金属原料としては、例え
ば、Pb原料にはPb(DPM)2、Pb(C254等、
Zr原料にはZr(DPM)4、Zr(t−OC494
等、Ti原料にはTi(I−OC374、Ti(DP
M)2(OCH32等が用いられる。
2. Description of the Related Art Conventionally, a sputtering method, a laser ablation (PLD) method, a molecular beam epitaxial (MBE) method, a metal organic chemical vapor deposition (MOCVD) method has been used as a method for producing a ferroelectric oxide thin film or a compound semiconductor thin film. ) Law,
The sol-gel method has been tried. MOCVD in particular
The method has excellent step coverage and is capable of forming a film on a large area, and can form a film at a relatively low temperature. Therefore, a thin film can be efficiently and easily grown.
When forming an oxide thin film, as a raw material for MOCVD, for example, a dipivaloylmethane (DPM) metal complex or the like, which has a relatively high vapor pressure due to sublimation at a temperature of 150 ° C. to 200 ° C., is used. Examples of the organometallic raw material of lead zirconate titanate (PZT), which is a ferroelectric oxide, include Pb (DPM) 2 and Pb (C 2 H 5 ) 4 as Pb raw materials.
Zr (DPM) 4 , Zr (t-OC 4 H 9 ) 4 is used as the Zr raw material.
, Ti (I-OC 3 H 7 ) 4 , Ti (DP
M) 2 (OCH 3 ) 2 and the like are used.

【0003】図3は、一般的なMOCVD装置の概略構
成を示す図である。
FIG. 3 is a diagram showing a schematic configuration of a general MOCVD apparatus.

【0004】図3に示す一般的なMOCVD装置は、大
きく分けて、複数の原料供給部と反応容器部の2つの部
分で構成されている。原料供給部は、導入側バルブ10
4、導出側バルブ105、原料容器106、キャリアガ
ス供給管108、有機金属原料ガス導出管109、マス
フローコントローラ110、オーブン111、バイパス
バルブ112、およびニードルバルブ113からなり、
有機金属原料を供給する部分である。反応容器部は、反
応容器114、酸素供給ライン115、基板ヒーター1
16、および原料ガス吐出口117からなり、輸送され
た有機金属を化学反応させて基板(不図示)上へ堆積さ
せて成膜する部分である。
The general MOCVD apparatus shown in FIG. 3 is roughly divided into a plurality of raw material supply sections and a reaction vessel section. The raw material supply unit is equipped with the inlet valve 10.
4, a discharge side valve 105, a raw material container 106, a carrier gas supply pipe 108, an organic metal raw material gas discharge pipe 109, a mass flow controller 110, an oven 111, a bypass valve 112, and a needle valve 113.
This is the part that supplies the organometallic raw material. The reaction container part includes a reaction container 114, an oxygen supply line 115, and a substrate heater 1.
16 and a raw material gas discharge port 117, which is a portion for chemically reacting the transported organic metal to deposit it on a substrate (not shown) to form a film.

【0005】MOCVD装置の作動時に、原料供給部か
ら原料供給が行われるときには、バイパスバルブ112
は閉じられ、導入側バルブ104と導出側バルブ105
は開けられている。そのため、マスフローコントローラ
110によって流量が制御された状態で、キャリアガス
供給管108を通って供給されてきたキャリアガスは、
導入側バルブ104を経て原料容器106内に導入され
る。そして、キャリアガスは、原料容器106内を通過
する間に原料容器106内の有機金属原料が混入して、
有機金属原料ガスに変わる。その有機金属原料ガスは、
導出側バルブ105を経て原料容器106の外に導出さ
れ、有機金属原料ガス導出管109を通り、ニードルバ
ルブ113を経て、原料ガス吐出口117から反応容器
114内に供給される。
When the raw material is supplied from the raw material supply unit during the operation of the MOCVD apparatus, the bypass valve 112 is used.
Are closed, and the inlet valve 104 and the outlet valve 105 are closed.
Is open. Therefore, the carrier gas supplied through the carrier gas supply pipe 108 in a state where the flow rate is controlled by the mass flow controller 110 is
It is introduced into the raw material container 106 via the introduction side valve 104. The carrier gas is mixed with the organometallic raw material in the raw material container 106 while passing through the raw material container 106,
Change to organometallic source gas. The organometallic source gas is
It is led out of the raw material container 106 via the outlet side valve 105, passes through the organometallic raw material gas outlet pipe 109, is passed through the needle valve 113, and is supplied into the reaction vessel 114 from the raw material gas discharge port 117.

【0006】上記のようなMOCVD装置では、作製す
る薄膜の組成や膜厚を安定させるためには、有機金属が
原料供給部から安定して供給される必要がある。
In the MOCVD apparatus as described above, in order to stabilize the composition and the film thickness of the thin film to be produced, it is necessary to stably supply the organic metal from the raw material supply section.

【0007】有機金属の安定供給に関して、MOCVD
法による固体原料供給方法及びその供給装置が特開平9
−40489号公報に記載されている。図4は、その固
体有機金属供給装置を示す断面図である。
MOCVD for stable supply of organic metal
Method for supplying solid raw material by the method and its supplying device
No. 40489. FIG. 4 is a cross-sectional view showing the solid organometallic supply device.

【0008】図4に示す原料供給装置は、固体原料であ
る有機金属が吸着された多孔質の吸着剤粒体218を収
容した原料容器206、原料容器206にキャリアガス
を供給するキャリアガス供給管208、原料容器206
から有機金属原料ガスを導出する有機金属原料ガス導出
管209、およびこれらを収容して加熱するオーブン2
11を有している。
The raw material supply device shown in FIG. 4 comprises a raw material container 206 containing a porous adsorbent granule 218 in which an organic metal which is a solid raw material is adsorbed, and a carrier gas supply pipe for supplying a carrier gas to the raw material container 206. 208, raw material container 206
Organometallic material gas outlet pipe 209 for deriving an organometallic material gas from the oven, and an oven 2 for accommodating and heating them
Have 11.

【0009】このような原料供給装置を用いた原料供給
方法は、固体原料を多孔質の吸着剤粒体218に吸着さ
せ、原料吸着後の粒体218をオーブン211による高
温雰囲気中に配された原料容器206内に収容し、この
粒体218に対してキャリアガスを通過させることによ
って行われる。キャリアガスが粒体218を通過する
と、粒体218に吸着していた固体原料がキャリアガス
中に混入し、有機金属原料ガスが生成される。そして、
この有機金属原料ガスが、有機金属原料ガス導出管20
9を経て供給される。
In the raw material supply method using such a raw material supply device, the solid raw material is adsorbed to the porous adsorbent granules 218, and the granules 218 after adsorbing the raw material are placed in a high temperature atmosphere by the oven 211. It is carried out by accommodating it in the raw material container 206 and passing a carrier gas through the granules 218. When the carrier gas passes through the granules 218, the solid raw material adsorbed on the granules 218 is mixed into the carrier gas to generate an organometallic raw material gas. And
This organometallic raw material gas is used as the organometallic raw material gas outlet pipe 20.
Supplied via 9.

【0010】また、特開2001−59178号公報に
は、化学気相成長法による原料供給装置及び方法が開示
されている。
Further, Japanese Patent Application Laid-Open No. 2001-59178 discloses a raw material supply device and method by a chemical vapor deposition method.

【0011】この供給装置は、原料容器内に固体原料が
広げられる多数段のシャーレ状部材と、キャリアガスの
拡散作用を有する間隙を画定する壁とを備えており、上
下多段に並べられたシャーレ状部材上に広げられた全て
の固体原料の表面を通過するようにキャリアガスを流す
ようになっている。
This supply device is provided with a large number of petri dish-shaped members in which a solid raw material is spread in a raw material container, and a wall which defines a gap having a diffusion action of carrier gas, and is arranged in a multi-tiered petri dish. The carrier gas is made to flow so as to pass through the surfaces of all the solid raw materials spread on the plate-shaped member.

【0012】[0012]

【発明が解決しようとする課題】上記の特開平9−40
489号公報に記載されたMOCVD法による固体原料
供給方法及び装置では、原料が新しい初期状態において
は、キャリアガスは固体原料を担持させた多孔質の吸着
剤粒体(担持体)中の全体に浸透しながら通過するの
で、所定の条件で所定の濃度の原料が混入したガスが安
定的に得られる。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
In the solid raw material supply method and apparatus by the MOCVD method described in Japanese Patent No. 489, in the initial state where the raw material is new, the carrier gas is entirely dispersed in the porous adsorbent granules (supporting body) supporting the solid raw material. Since the gas passes through while permeating, a gas in which a raw material having a predetermined concentration is mixed can be stably obtained under predetermined conditions.

【0013】しかし、この担持体はミクロ的に分布のあ
る多孔質の吸着剤粒体で形成されているため、この担持
体を何度か使用し、ある程度キャリアガスを担持体に通
過させた後には、担持体にガスの通過孔が形成され、キ
ャリアガスは通過孔内を優先的に通過するようになる。
担持体中にガスの通過孔が形成されると、原料はガスの
通過孔に沿った部分で主に消費されるようになる。キャ
リアガスが担持体中の全体に浸透しながら通過する当初
の状態に比べて、担持体にガスの通過孔が形成され、キ
ャリアガスがその通過孔を優先的に通過する状態の方
が、固体原料成分の濃度が低くなることから、通過した
ガス中に含まれる固体原料成分の濃度は経時的に変化し
てしまう。
However, since this carrier is formed of porous adsorbent granules having a microscopic distribution, this carrier is used several times and after a certain amount of carrier gas has passed through the carrier. In the carrier, gas passage holes are formed in the carrier, and the carrier gas preferentially passes through the passage holes.
When the gas passage holes are formed in the carrier, the raw material is mainly consumed in the portion along the gas passage holes. Compared to the initial state in which the carrier gas permeates the entire support while passing therethrough, a gas passage hole is formed in the support body, and the state in which the carrier gas preferentially passes through the passage hole is more solid. Since the concentration of the raw material component becomes low, the concentration of the solid raw material component contained in the gas that has passed changes with time.

【0014】上記のような理由から、キャリアガスの導
入条件を初期状態と同じにしておいた場合には、ガス中
の固体原料成分の濃度は、初期状態よりも経時的に低く
なってしまい、また、安定しなくなる。さらには、ガス
の流れやすさも変化してしまう。そのため、結果として
成膜後の物質の膜厚が薄くなったり、組成が変化したり
と、成膜結果にばらつきが発生してしまうという点が課
題となる。
For the above reasons, when the carrier gas introduction conditions are the same as in the initial state, the concentration of the solid raw material component in the gas becomes lower than that in the initial state over time, It also becomes unstable. Furthermore, the ease with which the gas flows will also change. Therefore, there is a problem in that variations in the film formation result occur such that the film thickness of the material after film formation becomes thin or the composition changes.

【0015】また、特開2001−59178号公報に
記載された構成では、原料容器内の原料を担持する部分
が多段のシャーレ状部材で構成されていることから、装
置の構造が複雑になり、かつ大型化する等、コスト的な
面が課題となる。
Further, in the structure described in Japanese Patent Application Laid-Open No. 2001-59178, since the part for supporting the raw material in the raw material container is composed of a multi-stage petri dish member, the structure of the apparatus becomes complicated, In addition, there is a problem in terms of cost such as an increase in size.

【0016】本発明は上記の従来技術が有する課題点に
鑑みて成されたものであり、その目的は、高い濃度の原
料ガスを長期間、効率よく安定的に得ることができる固
体有機金属の供給方法及びその供給装置を提供すること
にある。
The present invention has been made in view of the above-mentioned problems of the prior art, and an object thereof is to obtain a solid organic metal capable of obtaining a high-concentration raw material gas efficiently and stably for a long period of time. A supply method and a supply device thereof are provided.

【0017】[0017]

【課題を解決するための手段】上記目的を達成するた
め、本発明の固体有機金属の供給方法は、固体有機金属
を原料として基板上に薄膜を成膜する成膜装置に前記固
体有機金属を供給する固体有機金属の供給方法におい
て、前記固体有機金属を担持する担持体の一方の端面か
ら他方の端面へ貫通する多数の貫通穴の表面にそれぞれ
担持させた前記固体有機金属を前記固体有機金属が昇華
する温度の雰囲気中に保持し、前記各貫通穴にキャリア
ガスを通過させることにより前記キャリアガスに前記固
体有機金属が混入して得られる原料ガスを前記成膜装置
に供給することを特徴とする。
In order to achieve the above-mentioned object, a method for supplying a solid organic metal of the present invention is a solid metal organic material used as a raw material for forming a thin film on a substrate. In the method of supplying a solid organic metal, the solid organic metal supported on the surface of a large number of through holes penetrating from one end face of the carrier supporting the solid organic metal to the other end face, Is kept in an atmosphere at a temperature at which it sublimes, and a carrier gas is passed through each of the through holes to supply a raw material gas obtained by mixing the solid organic metal with the carrier gas to the film forming apparatus. And

【0018】上記本発明の固体有機金属の供給方法によ
れば、キャリアガスは予め所定の形状および大きさに形
成された貫通穴内を通るので、キャリアガスの流路は使
用開始の当初から一定となる。そのため、貫通穴を通る
キャリアガスが接触する有機金属原料の表面積は殆ど経
時変化せず、時間を経ても安定することから、貫通穴を
通るキャリアガスに含まれる原料の量も経時的に安定す
る。その結果、原料の濃度が高い原料ガスを長期間、効
率よく安定して供給することが可能になる。
According to the above-mentioned method for supplying a solid organic metal of the present invention, the carrier gas passes through the through hole formed in advance in a predetermined shape and size, so that the flow path of the carrier gas is constant from the beginning of use. Become. Therefore, the surface area of the organometallic raw material in contact with the carrier gas passing through the through-hole hardly changes with time and is stable over time, so that the amount of the raw material contained in the carrier gas passing through the through-hole also stabilizes with time. . As a result, it becomes possible to efficiently and stably supply the raw material gas having a high raw material concentration for a long period of time.

【0019】また、本発明の固体有機金属の供給装置
は、固体有機金属を担持させた担持体と、該担持体を収
容する容器と、該容器を少なくとも前記固体有機金属が
昇華する温度まで加熱する加熱手段と、前記容器内にキ
ャリアガスを通過させるキャリアガス搬送手段とを備え
ている固体有機金属の供給装置において、前記担持体は
前記キャリアガス搬送手段による前記キャリアガスの流
れ方向に関して上流側に位置する一方の端面から下流側
に位置する他方の端面に貫通する多数の貫通穴を有して
おり、前記固体有機金属は前記各貫通穴の表面に担持さ
れていることを特徴とする。
Further, the solid organometallic supply device of the present invention comprises a carrier carrying the solid organic metal, a container accommodating the carrier, and heating the container to at least a temperature at which the solid organic metal sublimes. In the solid-organic-metal-supplying device, which comprises heating means for heating and carrier gas carrying means for allowing carrier gas to pass through in the container, the carrier is upstream with respect to the flow direction of the carrier gas by the carrier gas carrying means. It has a large number of through-holes penetrating from one end face located on the other side to the other end face located on the downstream side, and the solid organic metal is carried on the surface of each of the through-holes.

【0020】上記本発明の固体有機金属の供給装置によ
れば、キャリアガスを予め所定の形状および大きさに形
成された貫通穴内を通すことができるので、キャリアガ
スの流路を使用開始の当初から一定にすることが可能に
なる。そのため、貫通穴を通るキャリアガスが接触する
有機金属原料の表面積が殆ど経時変化せず、時間を経て
も安定することから、貫通穴を通るキャリアガスに含ま
れる原料の量も経時的に安定させることが可能になる。
その結果、原料の濃度が高い原料ガスを長期間、効率よ
く安定して供給することができる。
According to the above-mentioned solid organic metal supply apparatus of the present invention, since the carrier gas can be passed through the through hole formed in advance in a predetermined shape and size, the carrier gas passage is initially used. It becomes possible to make it constant from. Therefore, since the surface area of the organometallic raw material which the carrier gas passing through the through-hole hardly changes with time and is stable over time, the amount of the raw material contained in the carrier gas passing through the through-hole also stabilizes over time. It will be possible.
As a result, the raw material gas having a high raw material concentration can be efficiently and stably supplied for a long period of time.

【0021】また、前記貫通穴の断面形状が円形または
多角形である構成としてもよい。
The cross-sectional shape of the through hole may be circular or polygonal.

【0022】さらに、前記貫通穴の直径が1mmから1
0mmの範囲である構成としてもよい。
Further, the diameter of the through hole is from 1 mm to 1 mm.
The configuration may be within the range of 0 mm.

【0023】さらには、前記貫通穴は互いに等間隔に配
置されている構成としてもよい。
Further, the through holes may be arranged at equal intervals.

【0024】また、前記担持体は、少なくとも常温から
前記温度の間では前記前記固体有機金属と反応せず、か
つ前記温度では耐熱性を有する材質からなる構成とする
ことが好ましい。
It is preferable that the carrier is made of a material that does not react with the solid organic metal at least between room temperature and the temperature and has heat resistance at the temperature.

【0025】[0025]

【発明の実施の形態】次に、本発明の実施形態について
図面を参照して説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, embodiments of the present invention will be described with reference to the drawings.

【0026】図1は本発明の一実施形態に係る固体有機
金属供給装置の概略構成を示す図、図2は図1に示した
固体有機金属供給装置を構成する有機金属担持体を示す
図である。図2において、同図(a)は有機金属担持体
の斜視図、同図(b)は同図(a)のA方向から有機金
属担持体を見た場合のいくつかの貫通孔を示す図であ
る。
FIG. 1 is a diagram showing a schematic structure of a solid organic metal supply apparatus according to an embodiment of the present invention, and FIG. 2 is a diagram showing an organic metal carrier constituting the solid organic metal supply apparatus shown in FIG. is there. 2, FIG. 2A is a perspective view of the organic metal carrier, and FIG. 2B is a diagram showing some through holes when the organic metal carrier is viewed from the direction A in FIG. Is.

【0027】本実施形態の固体有機金属供給装置は、一
方の端面から他方の端面に貫通する複数の貫通孔2の内
面に固体原料である有機金属原料3を担持した有機金属
担持体1と、この有機金属担持体1を収容した原料容器
6と、原料容器6にキャリアガスを供給するキャリアガ
ス供給管8と、原料容器6から有機金属原料ガスを導出
する有機金属原料ガス導出管9と、これらを収容して加
熱するオーブン11とを有している。さらに、原料容器
6内には、キャリアガス供給管8から供給されたキャリ
アガスを各貫通孔2内に均等に分配供給するシャワーヘ
ッド7が備えられている。
The solid metal-organic supply system of this embodiment comprises an organic metal carrier 1 carrying an organic metal raw material 3 as a solid raw material on the inner surfaces of a plurality of through holes 2 penetrating from one end face to the other end face, A raw material container 6 accommodating the organic metal carrier 1, a carrier gas supply pipe 8 for supplying a carrier gas to the raw material container 6, and an organic metal raw material gas discharge pipe 9 for discharging the organic metal raw material gas from the raw material container 6. It has the oven 11 which accommodates and heats these. Further, in the raw material container 6, there is provided a shower head 7 for uniformly distributing and supplying the carrier gas supplied from the carrier gas supply pipe 8 into each through hole 2.

【0028】キャリアガス供給管8と有機金属原料ガス
導出管9は、原料容器6内にキャリアガスを通過させる
キャリアガス搬送手段を構成している。また、有機金属
担持体1は、このキャリアガス搬送手段によるキャリア
ガスの流れ方向に対して上流側に一方の端面が位置し、
下流側に他方の端面が位置するように、原料容器6内に
設置されている。
The carrier gas supply pipe 8 and the organometallic raw material gas outlet pipe 9 constitute a carrier gas carrying means for passing the carrier gas into the raw material container 6. In addition, the organometallic carrier 1 has one end face located on the upstream side with respect to the flow direction of the carrier gas by the carrier gas carrier.
It is installed in the raw material container 6 such that the other end face is located on the downstream side.

【0029】本実施形態においても、図3に示した構成
と同様に、キャリアガス供給管8にはマスフローコント
ローラが設けられ、有機金属原料ガス導出管9にはニー
ドルバルブおよび原料ガス吐出口が設けられている(図
1および図2においては、いずれも不図示)。これらの
原料ガス吐出口は、基板ヒーターを内部に備え、また、
酸素供給ラインから酸素が供給されるように構成された
成膜装置を構成する反応容器(同様に不図示)内に有機
金属原料ガスを供給するようになっている。
Also in this embodiment, as in the configuration shown in FIG. 3, the carrier gas supply pipe 8 is provided with a mass flow controller, and the organometallic raw material gas outlet pipe 9 is provided with a needle valve and a raw material gas discharge port. (Not shown in FIGS. 1 and 2). These source gas discharge ports have a substrate heater inside, and
The organometallic raw material gas is supplied into a reaction container (also not shown) that constitutes a film forming apparatus configured to supply oxygen from an oxygen supply line.

【0030】本実施形態の固体有機金属供給装置では、
原料容器6がオーブン11中に入れられており、有機金
属原料3が昇華する温度まで加熱される。固体有機金属
原料3は、有機金属担持体1の貫通穴2の内表面に薄く
担持されている。
In the solid organometallic supply device of this embodiment,
The raw material container 6 is placed in an oven 11 and heated to a temperature at which the organometallic raw material 3 sublimes. The solid organometallic raw material 3 is thinly carried on the inner surface of the through hole 2 of the organometallic carrier 1.

【0031】有機金属担持体1の材質は、常温時及び加
熱状態時で有機金属原料3と反応せず、かつ有機金属原
料3の昇華温度以上の耐熱性を有するものであれば、い
ずれの材質であってもよい。その材質としては、特に、
熱的に安定なPTFEやポリイミド等のプラスチック、
アルミナ等のセラミックス、ガラス質、金属、焼結金
属、金属繊維、無機繊維、無機繊維強化金属等が適して
いる。なお、ここで「常温」とは有機金属担持体1を加
熱も冷却もしない周囲雰囲気の温度をいい、通常は約1
5℃の温度をいう。また、「加熱状態」とは有機金属担
持体1を有機金属原料3の昇華温度まで加熱した状態を
いう。
Any material can be used as the material of the organometallic carrier 1 as long as it does not react with the organometallic raw material 3 at room temperature and in a heated state and has heat resistance higher than the sublimation temperature of the organometallic raw material 3. May be As its material,
Thermally stable plastics such as PTFE and polyimide,
Ceramics such as alumina, glassy materials, metals, sintered metals, metal fibers, inorganic fibers, and inorganic fiber reinforced metals are suitable. The term "normal temperature" as used herein refers to the temperature of the ambient atmosphere in which the organic metal carrier 1 is neither heated nor cooled, usually about 1
Refers to a temperature of 5 ° C. Further, the “heating state” means a state in which the organic metal carrier 1 is heated to the sublimation temperature of the organic metal raw material 3.

【0032】本実施形態では貫通穴2の断面形状は円形
である。しかし、貫通穴2の断面形状はこれに限られ
ず、六角形をはじめとした多角形としてもよい。貫通穴
2の断面形状を六角形とした場合には、有機金属担持体
1の端面はハニカム形状となる。また、貫通穴2の直径
は1〜10mm程度とすることが好ましい。貫通穴2が
この程度の直径を有していれば、固体有機金属原料3が
貫通穴2内に詰まることを防止できる。
In this embodiment, the through hole 2 has a circular cross section. However, the sectional shape of the through hole 2 is not limited to this, and may be a polygon such as a hexagon. When the cross-sectional shape of the through hole 2 is hexagonal, the end surface of the organic metal carrier 1 has a honeycomb shape. The diameter of the through hole 2 is preferably about 1-10 mm. If the through hole 2 has such a diameter, it is possible to prevent the solid organic metal raw material 3 from clogging the through hole 2.

【0033】固体有機金属原料3は、原料粉末をTHF
(テトラヒドロフラン)等の有機溶媒に溶解し、これを
貫通穴2に流し込んで乾燥させることによって、有機金
属担持体1の貫通穴2に担持される。また、固体有機金
属原料3の粉末を溶解して液状にした後に貫通穴2内に
流し込み、これを冷却して固化させることによっても、
有機金属担持体1の貫通穴2に固体有機金属原料3を担
持させることができる。貫通穴2への固体有機金属原料
3の担持量は、原料3の濃度や、貫通穴2へ流し込む回
数等により調節する。
The solid organometallic raw material 3 is prepared by mixing raw material powder with THF.
It is dissolved in an organic solvent such as (tetrahydrofuran), poured into the through holes 2 and dried to be supported in the through holes 2 of the organic metal carrier 1. Alternatively, by melting the powder of the solid organometallic raw material 3 to form a liquid and then pouring it into the through hole 2 and cooling it to solidify,
The solid organic metal raw material 3 can be supported in the through holes 2 of the organic metal carrier 1. The amount of the solid organometallic raw material 3 carried on the through hole 2 is adjusted by the concentration of the raw material 3 and the number of times the raw material 3 is poured into the through hole 2.

【0034】有機金属担持体1の貫通穴2に流れるキャ
リアガスの量が不均一であると、供給装置からの原料の
供給量が不安定となる。そこで本実施形態では、この問
題を解決すべく、キャリアガス供給管8から供給された
キャリアガスが全ての貫通孔2内に均等に流入するよう
に上記のシャワーヘッド7が備えられている。シャワー
ヘッド7には各貫通穴2に対応して噴出口(不図示)が
形成されている。各噴出口の直径は0.5mm程度の大
きさを有している。
If the amount of carrier gas flowing through the through hole 2 of the organic metal carrier 1 is non-uniform, the amount of raw material supplied from the supply device becomes unstable. Therefore, in this embodiment, in order to solve this problem, the shower head 7 is provided so that the carrier gas supplied from the carrier gas supply pipe 8 flows into all the through holes 2 uniformly. Jet ports (not shown) are formed in the shower head 7 so as to correspond to the respective through holes 2. The diameter of each ejection port is about 0.5 mm.

【0035】なお、上記では原料容器6をオーブン11
中に収容して加熱する例を示したが、原料容器6(すな
わち有機金属担持体1)の加熱手段としては、この他に
オイルバス(不図示)等を用いることもできる。
In the above, the raw material container 6 is placed in the oven 11
Although an example in which the raw material container 6 (that is, the organic metal carrier 1) is housed in the inside and heated is shown, an oil bath (not shown) or the like may be used as the heating means other than this.

【0036】次に、本実施形態の供給装置を用いて固体
有機金属の供給を行い、基板上に成膜を行う動作につい
て説明する。
Next, the operation of supplying the solid organic metal by using the supply device of this embodiment to form a film on the substrate will be described.

【0037】本実施形態の供給装置を用いて固体有機金
属の供給を行うにあたっては、まず、キャリアガス供給
管8からオーブン11によって加熱された原料容器6内
にキャリアガスを導入する。このとき、キャリアガスの
流量はキャリアガス供給管8に設けられたマスフローコ
ントローラによって調節される。原料容器6内に導入さ
れたキャリアガスは、シャワーヘッド7を通り、固体有
機金属原料3を担持した有機金属担持体1の各貫通穴2
に均等に供給される。
When supplying the solid organic metal using the supply device of this embodiment, first, the carrier gas is introduced from the carrier gas supply pipe 8 into the raw material container 6 heated by the oven 11. At this time, the flow rate of the carrier gas is adjusted by the mass flow controller provided in the carrier gas supply pipe 8. The carrier gas introduced into the raw material container 6 passes through the shower head 7 and each through hole 2 of the organometallic carrier 1 carrying the solid organometallic raw material 3
Is evenly supplied to.

【0038】すると、貫通穴2の内表面に担持された有
機金属原料3がその表面にあるものから順に昇華し、キ
ャリアガスとともに有機金属原料ガス導出管9を通り、
反応容器内へと供給される。有機金属担持体1は複数の
貫通穴2が一方の端面から他方の端面へ貫通した構造を
しており、その貫通穴2は予め所定の形状および大きさ
に形成されているので、キャリアガスの流路は使用開始
の当初から一定である。そのため、貫通穴2を通るキャ
リアガスが接触する有機金属原料3の表面積は殆ど経時
変化せず、時間を経ても安定することから、貫通穴2を
通るキャリアガスに含まれる原料の量も経時的に安定す
る。その結果、原料の濃度が高い原料ガスを長期間、効
率よく安定して得ることが可能になる。
Then, the organometallic raw material 3 carried on the inner surface of the through hole 2 sublimes in that order from the surface thereof, and passes through the organometallic raw material gas outlet pipe 9 together with the carrier gas,
It is supplied into the reaction vessel. The organometallic carrier 1 has a structure in which a plurality of through holes 2 penetrates from one end face to the other end face, and since the through holes 2 are formed in a predetermined shape and size in advance, carrier gas The flow path is constant from the beginning of use. Therefore, the surface area of the organometallic raw material 3 that comes into contact with the carrier gas passing through the through hole 2 hardly changes with time, and is stable over time, so that the amount of the raw material contained in the carrier gas passing through the through hole 2 also changes with time. To be stable. As a result, it becomes possible to efficiently and stably obtain a raw material gas having a high raw material concentration for a long period of time.

【0039】さらに、有機金属担持体1の貫通穴2は直
線状に均等に形成されているので、キャリアガスは各貫
通穴2を無理なくスムーズに流れる。
Further, since the through holes 2 of the organic metal carrier 1 are linearly and evenly formed, the carrier gas flows smoothly in each through hole 2 without difficulty.

【0040】また、貫通穴2の直径が1〜10mm程度
と細いことから、貫通穴2を通るキャリアガスが有機金
属原料3に接触する機会が高くなるので、キャリアガス
中に多くの原料を含ませることができる。そのため、キ
ャリアガスが貫通穴2を通ることで得られる原料ガス中
の原料濃度が高くなり、より多くの原料を効率的に反応
容器内に供給することができる。
Further, since the diameter of the through hole 2 is as small as about 1 to 10 mm, the carrier gas passing through the through hole 2 has a high chance of coming into contact with the organic metal raw material 3, so that the carrier gas contains many raw materials. Can be made. Therefore, the raw material concentration in the raw material gas obtained by the carrier gas passing through the through holes 2 becomes high, and more raw material can be efficiently supplied into the reaction vessel.

【0041】このようにして反応容器内に送り込まれた
有機金属原料ガスは、高周波コイル等を有する基板ヒー
ターによって一定温度に保たれた基板上に供給される。
すると、有機金属原料ガスはそこで熱分解を起こし、有
機金属の配位子の離脱した金属部分が基板上に堆積し
て、目的とする薄膜が基板上に形成される。
The organometallic raw material gas thus fed into the reaction vessel is supplied onto the substrate kept at a constant temperature by the substrate heater having a high frequency coil or the like.
Then, the organometallic raw material gas undergoes thermal decomposition there, and the metal portion from which the ligand of the organometallic has desorbed is deposited on the substrate to form a target thin film on the substrate.

【0042】[0042]

【実施例】次に、上記に説明した本発明に係る固体有機
金属の供給装置及び方法の実施例を挙げ、PZT薄膜の
作製について具体的に説明する。
EXAMPLES Next, the production of a PZT thin film will be specifically described with reference to the examples of the apparatus and method for supplying a solid organic metal according to the present invention described above.

【0043】(実施例1)本実施例では、有機金属担持
体1に直径10cm、長さ10cmのアルミナ製の柱状
部材を用い、その有機金属担持体1には直径1mmの円
形の多数の貫通穴2を等間隔に形成した。この有機金属
担持体1は、まず直径1mmのステンレス製の多数の細
棒を束ねたものを用意し、その細棒同士の隙間にアルミ
ナの粉末を充填した後にこれを高温炉で焼結し、その
後、得られたアルミナ製の柱状部材からこれらの細棒を
抜き取ることによって形成した。
(Example 1) In this example, a columnar member made of alumina having a diameter of 10 cm and a length of 10 cm was used for the organic metal carrier 1, and the organic metal carrier 1 had a large number of circular holes having a diameter of 1 mm. The holes 2 were formed at equal intervals. The organometallic carrier 1 is prepared by bundling a large number of stainless steel thin rods having a diameter of 1 mm, filling the gaps between the thin rods with alumina powder, and sintering this in a high temperature furnace. After that, these thin rods were formed by pulling out from the obtained alumina columnar member.

【0044】有機金属原料3にはPZT(チタン酸ジル
コン酸鉛)を用いた。Pb原料にはPb(DPM)2
Zr原料にはZr(DPM)4、Ti原料にはTi(D
PM) 2(OCH32を用いた。有機金属原料3は、こ
れらの固体有機金属の原料粉末をTHF溶媒に溶解し、
これを有機金属担持体1の貫通穴2に流し込んで乾燥さ
せることによって、有機金属担持体1の貫通穴2に担持
させた。
The organic metal raw material 3 contains PZT (zirconium titanate).
Lead conate) was used. Pb (DPM) for Pb raw material2,
Zr as raw material for Zr (DPM)Four, Ti raw material is Ti (D
PM) 2(OCH3)2Was used. Organic metal raw material 3 is
These solid organometallic raw material powders are dissolved in a THF solvent,
This is poured into the through hole 2 of the organometallic carrier 1 and dried.
By carrying it, it is carried in the through hole 2 of the organometallic carrier 1.
Let

【0045】このようにして固体有機金属供給装置を作
製した。
In this way, a solid organometallic feeder was produced.

【0046】次いで、この供給装置によるそれぞれの有
機金属化合物の安定供給が可能であるか試験を行った。
まず、Pb(DPM)2、Zr(DPM)4、Ti(DP
M) 2(OCH32をそれぞれ担持した有機金属担持体
1を各々収容した3つの原料容器6を3つのオーブン1
1内にそれぞれ設置した。それぞれのオーブン11の設
定温度は、Pb(DPM)2を担持した有機金属担持体
1を収容した原料容器6が設置されたオーブン11を1
30℃、Zr(DPM)4を担持した有機金属担持体1
を収容した原料容器6が設置されたオーブン11を18
0℃、Ti(DPM)2(OCH32を担持した有機金
属担持体1を収容した原料容器6が設置されたオーブン
11を90℃とした。
Next, each of the supply devices
It was tested whether a stable supply of machine metal compounds was possible.
First, Pb (DPM)2, Zr (DPM)Four, Ti (DP
M) 2(OCH3)2Metal-organic support bearing each
3 raw material containers 6 each containing 1
It was installed in each one. Installation of each oven 11
Constant temperature is Pb (DPM)2-Supported organometallic support
1 the oven 11 in which the raw material container 6 containing 1 is installed
30 ° C, Zr (DPM)Four-Supported organometallic support 1
The oven 11 in which the raw material container 6 containing
0 ° C, Ti (DPM)2(OCH3)2Carrying organic gold
Oven in which a raw material container 6 containing the metal carrier 1 is installed
11 was set to 90 ° C.

【0047】次に、キャリアガス供給管8からこれらの
原料容器6内に、キャリアガスとして高純度のArガス
を導入した。それぞれの原料容器6では、有機金属担持
体1の貫通穴2に担持されていた各原料が昇華し、キャ
リアガスにその有機金属原料が含まれてなる有機金属原
料ガスが生成された。それらの有機金属原料ガスは、有
機金属原料ガス導出管9を通って反応容器内へと供給さ
れた。
Next, high-purity Ar gas was introduced as a carrier gas into the raw material containers 6 from the carrier gas supply pipe 8. In each raw material container 6, each raw material carried in the through hole 2 of the organometallic carrier 1 was sublimated, and an organometallic raw material gas containing the organometallic raw material in the carrier gas was generated. The organometallic raw material gas was supplied into the reaction vessel through the organometallic raw material gas outlet pipe 9.

【0048】反応容器内にはMgOからなる基板を設置
し、その基板は基板ヒーターで450℃に保温した。各
原料容器6から供給された有機金属原料ガスは基板上で
熱分解を起こし、有機金属の配位子が離脱した各種の金
属部分が基板上に堆積して、目的とするPZT薄膜が基
板上に形成された。
A substrate made of MgO was placed in the reaction vessel, and the substrate was kept at 450 ° C. by a substrate heater. The organometallic raw material gas supplied from each raw material container 6 undergoes thermal decomposition on the substrate, various metal parts from which the organometallic ligand is released are deposited on the substrate, and the desired PZT thin film is deposited on the substrate. Formed in.

【0049】この供給方法によれば、原料3が有機金属
担持体1から無くなるまでの長期間にわたって、同様の
組成及び膜厚のPZT薄膜が得られた。これにより、本
実施例による原料供給は安定性に優れていることが確認
された。
According to this supply method, a PZT thin film having the same composition and film thickness was obtained for a long period of time until the raw material 3 disappeared from the organic metal carrier 1. From this, it was confirmed that the raw material supply according to this example had excellent stability.

【0050】(実施例2)本実施例では、有機金属担持
体1をアルミナの絶縁管を用いて作製した。具体的に
は、有機金属担持体1を、直径約1mm、長さ10cm
のアルミナ製の多数の中空絶縁管を均等に束ねて作製し
た。本実施例の固体有機金属供給装置の構成および供給
方法は、有機金属担持体1の作製方法以外は実施例1と
同様とした。
(Example 2) In this example, the organometallic carrier 1 was manufactured using an alumina insulating tube. Specifically, the organic metal carrier 1 has a diameter of about 1 mm and a length of 10 cm.
Was manufactured by bundling a number of hollow insulating tubes made of alumina. The configuration and supply method of the solid organic metal supply apparatus of this example were the same as those of Example 1 except for the method for producing the organic metal carrier 1.

【0051】この供給装置を用いてこの実施例1と同様
に試験したところ、実施例1と同様に、長期間にわたっ
て同様の組成及び膜厚のPZT薄膜が得られた。これに
より、本実施例による原料供給は安定性に優れているこ
とが確認された。
When a test was conducted in the same manner as in Example 1 using this supplying apparatus, a PZT thin film having the same composition and film thickness as in Example 1 was obtained over a long period of time. From this, it was confirmed that the raw material supply according to this example had excellent stability.

【0052】(実施例3)本実施例では、有機金属担持
体1に直径10cm、長さ10cmのアルミナ製の柱状
部材を用い、その有機金属担持体1には中心を通る対角
線の長さが2mmの正八角形の多数の貫通穴2を等間隔
に形成した。この有機金属担持体1は、まず中心を通る
対角線の長さが2mmの正八角形のステンレス製の多数
の細棒を束ねたものを用意し、その細棒同士の隙間に加
熱溶融させたポリイミドを充填した後にこれを冷却し、
その後、得られた柱状部材からこれらの細棒を抜き取る
ことによって形成した。本実施例の固体有機金属供給装
置の構成および供給方法は、有機金属担持体1の作製方
法以外は実施例1と同様とした。
Example 3 In this example, a columnar member made of alumina having a diameter of 10 cm and a length of 10 cm was used for the organometallic carrier 1, and the organometallic carrier 1 had a diagonal line passing through the center thereof. A large number of 2 mm regular octagonal through holes 2 were formed at equal intervals. The organometallic carrier 1 is prepared by bundling a large number of regular octagonal stainless steel thin rods having a diagonal length of 2 mm passing through the center thereof. Cool it after filling,
After that, these thin rods were formed by extracting them from the obtained columnar member. The configuration and supply method of the solid organic metal supply apparatus of this example were the same as those of Example 1 except for the method for producing the organic metal carrier 1.

【0053】この供給装置を用いてこの実施例1と同様
に試験したところ、実施例1と同様に、長期間にわたっ
て同様の組成及び膜厚のPZT薄膜が得られた。これに
より、本実施例による原料供給は安定性に優れているこ
とが確認された。
When the same test as in Example 1 was conducted using this supplying apparatus, a PZT thin film having the same composition and film thickness was obtained for a long period of time as in Example 1. From this, it was confirmed that the raw material supply according to this example had excellent stability.

【0054】(実施例4)本実施例では、固体有機金属
であるPb(DPM)2、Zr(DPM)4、Ti(DP
M)2(OCH32の原料粉末を加熱溶融させて液状に
した後に貫通穴2に流し込み、その後冷却して固化させ
ることによって、有機金属原料3を有機金属担持体1の
貫通穴2に担持させた。本実施例の固体有機金属供給装
置の構成および供給方法は、有機金属原料3の担持方法
以外は実施例1と同様とした。
Example 4 In this example, Pb (DPM) 2 , Zr (DPM) 4 , Ti (DP), which are solid organic metals, are used.
The raw material powder of M) 2 (OCH 3 ) 2 is heated and melted to form a liquid, which is then poured into the through hole 2 and then cooled and solidified, so that the organic metal raw material 3 is introduced into the through hole 2 of the organic metal carrier 1. It was supported. The configuration and supply method of the solid organic metal supply apparatus of this example were the same as in Example 1 except for the method of supporting the organic metal raw material 3.

【0055】この供給装置を用いてこの実施例1と同様
に試験したところ、実施例1と同様に、長期間にわたっ
て同様の組成及び膜厚のPZT薄膜が得られた。これに
より、本実施例による原料供給は安定性に優れているこ
とが確認された。
When a test was conducted in the same manner as in Example 1 using this supplying apparatus, a PZT thin film having the same composition and film thickness as in Example 1 was obtained for a long period of time. From this, it was confirmed that the raw material supply according to this example had excellent stability.

【0056】[0056]

【発明の効果】以上説明したように、本発明は、担持体
の一方の端面から他方の端面へ貫通する多数の貫通穴の
表面にそれぞれ固体有機金属を担持させ、キャリアガス
をその貫通穴に通して原料ガスを得るように構成されて
いるので、貫通穴を通るキャリアガスが接触する有機金
属原料の表面積が殆ど経時変化することがなく、原料の
濃度が高い原料ガスを長期間、効率よく安定して供給す
ることができる。
As described above, according to the present invention, the solid organic metal is carried on the surface of each of the through holes penetrating from one end surface of the carrier to the other end surface, and the carrier gas is introduced into the through holes. Since it is configured to obtain the raw material gas through the through-hole, the surface area of the organometallic raw material in contact with the carrier gas passing through the through-hole hardly changes with time, and the raw material gas having a high raw material concentration can be efficiently used for a long period of time. It can be stably supplied.

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

【図1】本発明の一実施形態に係る固体有機金属供給装
置の概略構成を示す図である。
FIG. 1 is a diagram showing a schematic configuration of a solid organometallic supply device according to an embodiment of the present invention.

【図2】図1に示した固体有機金属供給装置を構成する
有機金属担持体を示す図である。
FIG. 2 is a diagram showing an organic metal carrier that constitutes the solid organic metal supply device shown in FIG.

【図3】一般的なMOCVD装置の概略構成を示す図で
ある。
FIG. 3 is a diagram showing a schematic configuration of a general MOCVD apparatus.

【図4】従来の固体有機金属供給装置を示す断面図であ
る。
FIG. 4 is a cross-sectional view showing a conventional solid organic metal supply device.

【符号の説明】[Explanation of symbols]

1 有機金属担持体 2 貫通穴 3 固体有機金属原料 4 導入側バルブ 5 導出側バルブ 6 原料容器 7 シャワーヘッド 8 キャリアガス供給管 9 有機金属原料ガス導出管 11 オーブン 1 Organic metal support 2 through holes 3 Solid metal raw materials 4 Introductory valve 5 Outlet valve 6 raw material containers 7 shower head 8 Carrier gas supply pipe 9 Organic metal source gas outlet pipe 11 oven

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4K030 AA11 AA16 BA01 BA22 BA42 BA46 CA05 EA01 5F045 AA04 AB31 AC07 AC16 BB01 BB08 EE02    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4K030 AA11 AA16 BA01 BA22 BA42                       BA46 CA05 EA01                 5F045 AA04 AB31 AC07 AC16 BB01                       BB08 EE02

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 固体有機金属を原料として基板上に薄膜
を成膜する成膜装置に前記固体有機金属を供給する固体
有機金属の供給方法において、 前記固体有機金属を担持する担持体の一方の端面から他
方の端面へ貫通する多数の貫通穴の表面にそれぞれ担持
させた前記固体有機金属を前記固体有機金属が昇華する
温度の雰囲気中に保持し、前記各貫通穴にキャリアガス
を通過させることにより前記キャリアガスに前記固体有
機金属が混入して得られる原料ガスを前記成膜装置に供
給することを特徴とする固体有機金属の供給方法。
1. A method for supplying a solid organic metal to a film forming apparatus for forming a thin film on a substrate from a solid organic metal as a raw material, comprising: To hold the solid organic metal supported on the surface of each of the through holes penetrating from one end face to the other end face in an atmosphere at a temperature at which the solid organic metal sublimes, and to pass a carrier gas through each of the through holes. A method for supplying solid organic metal, comprising: supplying a raw material gas obtained by mixing the solid organic metal with the carrier gas to the film forming apparatus.
【請求項2】 固体有機金属を担持させた担持体と、該
担持体を収容する容器と、該容器を少なくとも前記固体
有機金属が昇華する温度まで加熱する加熱手段と、前記
容器内にキャリアガスを通過させるキャリアガス搬送手
段とを備えている固体有機金属の供給装置において、 前記担持体は前記キャリアガス搬送手段による前記キャ
リアガスの流れ方向に関して上流側に位置する一方の端
面から下流側に位置する他方の端面に貫通する多数の貫
通穴を有しており、前記固体有機金属は前記各貫通穴の
表面に担持されていることを特徴とする固体有機金属の
供給装置。
2. A carrier carrying a solid organic metal, a container accommodating the carrier, a heating means for heating the container at least to a temperature at which the solid organic metal sublimes, and a carrier gas in the container. In the solid-organic metal supply device comprising a carrier gas transporting means for passing the carrier gas, the carrier is located downstream from one end face located upstream in the flow direction of the carrier gas by the carrier gas transporting means. A plurality of through holes penetrating the other end surface of the solid organic metal are carried, and the solid organic metal is carried on the surface of each of the through holes.
【請求項3】 前記貫通穴の断面形状が円形または多角
形である、請求項2に記載の固体有機金属の供給装置。
3. The solid organometallic supply device according to claim 2, wherein the through hole has a circular or polygonal cross-sectional shape.
【請求項4】 前記貫通穴の直径が1mmから10mm
の範囲である、請求項2または3に記載の固体有機金属
の供給装置。
4. The diameter of the through hole is 1 mm to 10 mm.
The solid organometallic supply device according to claim 2 or 3, which is in the range.
【請求項5】 前記貫通穴は互いに等間隔に配置されて
いる、請求項2から4のいずれか1項に記載の固体有機
金属の供給装置。
5. The solid organometallic supply device according to claim 2, wherein the through holes are arranged at equal intervals.
【請求項6】 前記担持体は、少なくとも常温から前記
温度の間では前記前記固体有機金属と反応せず、かつ前
記温度では耐熱性を有する材質からなる、請求項2から
5のいずれか1項に記載の固体有機金属の供給装置。
6. The support according to claim 2, wherein the carrier is made of a material which does not react with the solid organic metal at least between room temperature and the temperature and has heat resistance at the temperature. The solid-organic metal supply device according to.
JP2002066953A 2002-03-12 2002-03-12 Feeding method of solid organic metal, and its feeder Pending JP2003273093A (en)

Priority Applications (1)

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Publication Number Publication Date
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Family

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Country Link
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007520052A (en) * 2003-09-30 2007-07-19 東京エレクトロン株式会社 A method of depositing a metal layer from a metal-carbonyl precursor.
WO2007057631A3 (en) * 2005-11-17 2008-05-29 Sigma Aldrich Co Improved bubbler for the transportation of substances by a carrier gas
US7635395B2 (en) 2002-09-24 2009-12-22 Fujitsu Limited Solid material gasification method
US9297071B2 (en) 2009-11-02 2016-03-29 Sigma-Aldrich Co. Llc Solid precursor delivery assemblies and related methods
CN114616356A (en) * 2019-11-05 2022-06-10 东京毅力科创株式会社 Apparatus for processing substrate, raw material box, method for processing substrate and method for manufacturing raw material box
WO2023037880A1 (en) * 2021-09-08 2023-03-16 東京エレクトロン株式会社 Feedstock supply device
JP7432722B2 (en) 2019-11-14 2024-02-16 インテグリス・インコーポレーテッド Densified solid preform for sublimation

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7635395B2 (en) 2002-09-24 2009-12-22 Fujitsu Limited Solid material gasification method
JP2007520052A (en) * 2003-09-30 2007-07-19 東京エレクトロン株式会社 A method of depositing a metal layer from a metal-carbonyl precursor.
WO2007057631A3 (en) * 2005-11-17 2008-05-29 Sigma Aldrich Co Improved bubbler for the transportation of substances by a carrier gas
JP2009516079A (en) * 2005-11-17 2009-04-16 シグマ−アルドリッチ・カンパニー Bubbler for transferring material by carrier gas
CN101310042B (en) * 2005-11-17 2011-06-29 西格玛-奥吉奇公司 Improved bubbler for the transportation of substances by a carrier gas
US8272626B2 (en) 2005-11-17 2012-09-25 Sigma-Aldrich Co. Llc Bubbler for the transportation of substances by a carrier gas
KR101303271B1 (en) 2005-11-17 2013-09-03 시그마 알드리치 컴퍼니 엘엘씨 Improved bubbler for the transportation of substances by a carrier gas
US9297071B2 (en) 2009-11-02 2016-03-29 Sigma-Aldrich Co. Llc Solid precursor delivery assemblies and related methods
CN114616356A (en) * 2019-11-05 2022-06-10 东京毅力科创株式会社 Apparatus for processing substrate, raw material box, method for processing substrate and method for manufacturing raw material box
JP7432722B2 (en) 2019-11-14 2024-02-16 インテグリス・インコーポレーテッド Densified solid preform for sublimation
WO2023037880A1 (en) * 2021-09-08 2023-03-16 東京エレクトロン株式会社 Feedstock supply device

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