JPH0226017A - Method of producing saturated vapor of organometal compound in organometallic vapor growth - Google Patents

Method of producing saturated vapor of organometal compound in organometallic vapor growth

Info

Publication number
JPH0226017A
JPH0226017A JP17489388A JP17489388A JPH0226017A JP H0226017 A JPH0226017 A JP H0226017A JP 17489388 A JP17489388 A JP 17489388A JP 17489388 A JP17489388 A JP 17489388A JP H0226017 A JPH0226017 A JP H0226017A
Authority
JP
Japan
Prior art keywords
cylinder
inner tube
carrier gas
organometallic compound
organometallic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP17489388A
Other languages
Japanese (ja)
Other versions
JPH0531293B2 (en
Inventor
Akira Yamane
山根 昭
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.)
Tosoh Finechem Corp
Original Assignee
Tosoh Finechem 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 Tosoh Finechem Corp filed Critical Tosoh Finechem Corp
Priority to JP17489388A priority Critical patent/JPH0226017A/en
Publication of JPH0226017A publication Critical patent/JPH0226017A/en
Publication of JPH0531293B2 publication Critical patent/JPH0531293B2/ja
Granted legal-status Critical Current

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  • Semiconductor Lasers (AREA)

Abstract

PURPOSE:To facilitate control of the composition of a single crystal thin film by a method wherein an inner tube which is directly connected to an exhaust outlet and has a disperser at its bottom is inserted into a cylinder and both the cylinder and the inner tube are filled with organometal compound and carrier gas introduced into the cylinder through an introducing inlet is discharged out of the cylinder. CONSTITUTION:An introducing inlet and an exhaust outlet for carrier gas are provided in the upper part A2 of a cylinder A and an inner tube G directly connected to the exhaust outlet is inserted into the cylinder A. Both the cylinder A and the inner tube G are filled with an organometallic compound and the carrier gas is introduced into the cylinder A through the introducing inlet and discharged out of the cylinder A from the bottom of the inner tube G and through the inner tube G. Therefore, a constant supply rate of the organometallic compound can be obtained stably for a long time without relying upon the filling rate of the solid organometal compound, the flow rate of the carrier gas and so forth. With this constitution, the composition of a single crystal thin film can be controlled.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は半導体用固体有機金属化合物の有機金属気相成
長(Metal 0roanic Chemical 
VaporDeposition : )10−CVD
)法における有機金属化合物の飽和蒸気生成方法に関す
るものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to metal organic chemical vapor phase epitaxy of solid organometallic compounds for semiconductors.
VaporDeposition: )10-CVD
) method for producing saturated vapor of organometallic compounds.

〔従来の技術〕[Conventional technology]

現在、半導体レーザー等の製造に必たり効率よく量産化
できる方法として有機金属化合物を用いる)10−CV
D法は良く知られている。
Currently, organometallic compounds are used as a method that can be efficiently mass-produced in the production of semiconductor lasers, etc.) 10-CV
D method is well known.

No−CVD法とは、有機金属化合物と通常水素ガス等
のキャリア−ガスを接触せしめて有機金属化合物の飽和
蒸気として高温下にあるウェーハー上に送り、ウェーハ
ー上で原料ガスと反応させ、この反応により生成する化
合物の単結晶薄膜を成長させる方法である。更に詳しく
は、つニーバー上に例えば(CI−13)sGaとAs
)13のガスを高温下にあるウェーハー上で反応させ、
下記反応式 △ (CH3)3 Ga+ASH:+  −m=−→GaA
s+30H4 によりGaASの単結晶薄膜を成長させる方法でおる。
In the No-CVD method, an organometallic compound is brought into contact with a carrier gas such as hydrogen gas, and the saturated vapor of the organometallic compound is sent onto a wafer under high temperature, and is reacted with the raw material gas on the wafer. This is a method of growing a single crystal thin film of a compound produced by. More specifically, for example, (CI-13) sGa and As are placed on the kneebar.
) 13 gases are reacted on a wafer under high temperature,
The following reaction formula △ (CH3)3 Ga+ASH:+ -m=-→GaA
The method is to grow a GaAS single crystal thin film using s+30H4.

)10−CVD法においては、シリンダーに充填された
有機金属化合物をキャリア−ガスで反応炉へ運び結晶成
長させている。
) In the 10-CVD method, an organometallic compound filled in a cylinder is transported to a reactor using a carrier gas to grow crystals.

本発明者らは先に特開昭63−11598号に開示され
たように第3図に示す通り、キャリア−ガス入口管(1
)に接続するシリンダー(2)の中心軸を通るキャリア
−ガス導入管(3)の下部に分散器(フィルター)(4
)を取り付けかつ、シリンダー(2)下部(2−1)は
シリンダー上部(2−2)に比べその内径を狭めた狭径
部とし、しかも該狭径部の上に傾斜部(2−3)を備え
導入管(3)より分散器(4)を経てシリンダー(2)
の底部に導入されたキャリア−ガスは有機金属化合物の
充填されたシリンダー(2)内を上昇する間に有機金属
化合物の蒸気で飽和され、排出口(5)からシリンダー
外に排出される)10−CVD法用シリンダーを提案し
た。
As previously disclosed in Japanese Patent Application Laid-Open No. 63-11598, the present inventors constructed a carrier-gas inlet pipe (1) as shown in FIG.
) A disperser (filter) (4
), and the lower part (2-1) of the cylinder (2) has a narrower inner diameter than the upper part of the cylinder (2-2), and an inclined part (2-3) is attached above the narrowed part. from the introduction pipe (3) to the cylinder (2) via the disperser (4)
The carrier gas introduced into the bottom of the cylinder (2) becomes saturated with the vapor of the organometallic compound while rising inside the cylinder (2) filled with the organometallic compound, and is discharged from the cylinder through the outlet (5). -We proposed a cylinder for CVD method.

該提案によれば、特に固体有機金属化合物の場合効果が
認められるが、それでも尚不十分であることが分った。
Although this proposal is particularly effective in the case of solid organometallic compounds, it has been found that it is still insufficient.

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

上記の提案では有機金属化合物としてトリメチルインジ
ウム(TMIn>を用い、充填量を5〜50gの間で不
連続的に変えTM I n供給量を求めている。
In the above proposal, trimethylindium (TMIn> is used as the organometallic compound, and the amount of TMIn supplied is determined by discontinuously changing the filling amount between 5 and 50 g.

この方法によると各TMIn量における供給試験開始時
のTMInの充填状態は極めて良くまた、該提案の実施
例の如くキャリア−ガス流量が大きくなくしかも3時間
という比較的短時間のため、供給試験終了時のTM I
 nの充填状態は殆ど変化しないことから試験中TM 
I nとキャリア−ガスとの接触は十分であり従って、
容易に飽和に達し、その結果として供給量は一定値を示
していた。
According to this method, the filling state of TMIn at the start of the supply test for each TMIn amount is extremely good, and unlike the proposed embodiment, the carrier gas flow rate is not large and the supply test is completed within a relatively short time of 3 hours. Time TM I
Since the filling state of n hardly changes, TM during the test
The contact between In and the carrier gas is sufficient so that
Saturation was easily reached, and as a result, the supply amount remained constant.

しかし、実際の使用法に即した供給試験即ち、シリンダ
ーに所定量のTM I nを充填し供給試験を長時間連
続的に行ってみると、先に述べた様に比較的短時間では
充填状態の変化は殆ど見られないものの、時間の経過と
共にフィルターの回りのTM I nが空洞化しガス流
路ができるためTM I nとキャリア−ガスの接触が
次第に不十分となり、その結果供給量が徐々に低下し単
結晶薄膜の組成コントロールができ難いという欠点が明
らかになった。
However, when we conduct a supply test in accordance with actual usage, that is, fill a cylinder with a predetermined amount of TM In and conduct a supply test continuously over a long period of time, we find that the filled state does not reach the filled state in a relatively short period of time, as mentioned earlier. Although almost no change is observed, as time passes, the TM I n around the filter becomes hollow and a gas flow path is formed, so the contact between the TM I n and the carrier gas gradually becomes insufficient, and as a result, the supply amount gradually decreases. The disadvantage of this study was that it was difficult to control the composition of single-crystal thin films.

(課題を解決するための手段〕 そこで本発明者は更に改良するため種々検討の結果シリ
ンダー上部にキャリア−ガスの導入口および排出口を夫
々設け、この排出口に直結した内管をシリンダー内に挿
入しこれらのシリンダーおよび内管の双方に有機金属化
合物を充填して、キャリア−ガスを上記導入口よりシリ
ンダー内に送入し、内管底部より内管を通って排出口よ
り排出せしめることによりキャリア−ガス流量が大きい
場合においても極めて良好な結果が得られることを発見
し本発明を完成するに至った。
(Means for Solving the Problems) Therefore, in order to further improve the problem, the inventor of the present invention conducted various studies and established an inlet and an outlet for the carrier gas at the top of the cylinder, respectively, and inserted an inner pipe directly connected to the outlet into the cylinder. By inserting the cylinder and filling both the cylinder and the inner tube with an organometallic compound, the carrier gas is introduced into the cylinder from the above-mentioned inlet, passes through the inner tube from the bottom of the inner tube, and is discharged from the outlet. The present inventors have discovered that extremely good results can be obtained even when the carrier gas flow rate is large, and have completed the present invention.

即ち、本発明の要旨とする所は有機金属気相成長用シリ
ンダーの上部に夫々キャリア−ガスの導入口および排出
口を設け、この排出口に直結しかつ底部に分散器を装備
した内管を該シリンダー内に挿入し、これらのシリンダ
ーおよび内管内の双方に有機金属化合物を夫々充填して
前記導入口よりシリンダー内に送入したキャリア−ガス
をシリンダー内底部より上記の分散器を経て内管を通り
前記の排出口からシリンダー外に排出せしめることを特
徴とする有機金属気相成長法における有機金属化合物の
飽和蒸気生成方法に存し、これにより所期の目的を収め
たものである。
That is, the gist of the present invention is to provide an inlet and an outlet for carrier gas at the top of a cylinder for organometallic vapor phase growth, and to provide an inner tube directly connected to the outlet and equipped with a disperser at the bottom. The carrier gas is inserted into the cylinder, filled with an organometallic compound in both the cylinder and the inner tube, and is fed into the cylinder from the inlet. The present invention provides a method for producing saturated vapor of an organometallic compound in an organometallic vapor phase epitaxy method, which is characterized by discharging the vapor from the cylinder through the above-mentioned outlet, thereby achieving the intended purpose.

尚、本発明に使用する分散器はポーラスなものであれば
どんなものでもよく、例えばプラスチックボールフィル
ターでもセルボールデイスりでもよく、また材質的にス
テンレススティールとかセラミックス製のものでも、ま
た繊維状のものでも、耐久性があり、はぼ均一な1〜1
00μの微細なポーラスなものならよい。
The disperser used in the present invention may be any porous material, such as a plastic ball filter or a cell ball disk, or may be made of stainless steel or ceramics, or may be made of fibrous material. Even if it is durable, it is uniform 1~1
A fine porous material with a diameter of 00 μm is sufficient.

〔作 用〕[For production]

本発明者らが特開昭63−11598号に開示したシリ
ンダーについては第3図によって説明したが、ガラスで
製作したこのシリンダーにTMInを入れ窒素ガスを毎
分500 idの割合で連続的に導入したところ、TM
I nの使用量が約10%の時点でフィルターの回りに
TMI nの空洞化が観察され供給量が低下し始めた。
The cylinder disclosed by the present inventors in JP-A No. 63-11598 was explained with reference to FIG. 3, and TMIn was placed in this cylinder made of glass, and nitrogen gas was continuously introduced at a rate of 500 id per minute. Then, TM
When the amount of In used was about 10%, cavitation of TMI n was observed around the filter and the amount supplied began to decrease.

そこで種々試験の結果、本発明方法で試験してみると長
時間均等量のガスが良好に得られ、従ってウェーハー上
に所定の単結晶薄膜を生成することが分かった。これは
、末鎖和分を内管に充填したTM I nが補足する作
用によるものと考えられる。この場合、キャリア−ガス
のシリンダー内における線速度は遅い程好ましいが、特
に限定されることはなくキャリア−ガス流量に合わせて
シリンダー径を決めることが望ましい。また、内管につ
いては固体有機金属化合物の充填のし易さを考慮すると
シリンダーの大きざにもよるが、一般的にはその直径が
5J11111以上が適当である。なお、シリンダー下
部はシリンダー上部に比べその内径を狭めた狭径部とし
ても良く、また、該狭径部の上に傾斜部を備えても何ら
差しつかえない。
As a result of various tests, it has been found that when tested using the method of the present invention, a uniform amount of gas can be obtained satisfactorily over a long period of time, thereby producing a desired single crystal thin film on a wafer. This is thought to be due to the action of TM I n, which fills the inner tube, supplementing the terminal chain fraction. In this case, the linear velocity of the carrier gas in the cylinder is preferably as slow as possible, but there is no particular limitation, and it is desirable to determine the diameter of the cylinder in accordance with the flow rate of the carrier gas. In addition, considering the ease of filling the solid organometallic compound with respect to the inner tube, it is generally appropriate that the diameter thereof is 5J11111 or more, although it depends on the size of the cylinder. Note that the lower part of the cylinder may be a narrow diameter part whose inner diameter is narrower than that of the upper part of the cylinder, and there is no problem even if an inclined part is provided above the narrow diameter part.

更に、シリンダー全体は丸形に限定されることはない。Furthermore, the entire cylinder is not limited to a round shape.

〔実施例〕〔Example〕

第1図および第2図は本発明方法に使用される有機金属
気相成長用シリンダーを示すが、たで型円筒状のシリン
ダー(A)の上部にはその円形周辺部にシリンダー(A
)内に有機金属化合物を装入するための有機金属化合物
の投入口上に垂直に立上る管路(B)とその円形中心部
に内管(G)に有機金属化合物を装入するための有機金
属化合物の投入口(C)が夫々設けられ、又その円形周
辺部にはキャリア−ガスの導入口上に垂直に立上るキャ
リア−ガスの導入管路(D)とがあり、この導入管路(
D)よりコック(E)を介してシリンダー(A)内にキ
ャリア−ガスが導入される。後者の有機金属化合物の投
入口(C)には有機金属化合物充填用の内管(G)が直
結しシリンダー(A)内をその中心を貫いて上部より底
部近くまで挿入されており、内管(G)の下端には分散
器(フィルター>  [NUPROFILTER100
μ(ヌプロ フィルター) (ヌプロ カンパニイ:4
800  イースト345ストリート、ウイラウクバイ
、オハイオ 44094製 4800 East 34
5thStreet、 Willonohby、 0h
io 44094) ] (H)が設けである。後者の
有機金属化合物の投入口(C)はキャアーガスの排出口
も兼ね、これにシリンダー(^)の上部よりその円形周
辺部に屈曲してから垂直に立上るキャリア−ガス排出管
路(F)が接続されコック(I)を経て有機金属化合物
の飽和蒸気を含むキャリア−ガスを排出するようになっ
ている。そこで前記のコック(E)を介して管路(D)
内に送入されたキャリア−ガスは、矢印で示す様に有機
金属化合物の充填されたシリンダー(A)内に導入され
てシリンダー(A)の底部に至るが、その間に有機金属
化合物の蒸気を含んだキャリア−ガスは、次いで分散器
(H)を通して矢印で示す様に同じく有機金属化合物の
充填された内管(G)内を上昇し、ここで有機金属化合
物の飽和蒸気を含んで排出管路(F)を経てコック(I
)を通して排出される様になっている。
1 and 2 show cylinders for organometallic vapor phase growth used in the method of the present invention.
) and a pipe (B) vertically rising above the inlet for organometallic compounds for charging the organometallic compound into the inner pipe (G). Each metal compound inlet (C) is provided, and a carrier-gas inlet (D) is provided on the circular periphery of the inlet, and the carrier-gas inlet (D) rises vertically above the carrier-gas inlet.
Carrier gas is introduced into the cylinder (A) from D) via the cock (E). An inner pipe (G) for filling the organometallic compound is directly connected to the latter organometallic compound inlet (C), and is inserted through the center of the cylinder (A) from the top to near the bottom. At the lower end of (G) is a disperser (filter > [NUPROFILTER100
μ (Nupro Filter) (Nupro Company: 4
800 East 345 Street, Willaukbai, Ohio 44094 4800 East 34
5th Street, Willonohby, 0h
io 44094)] (H) is provided. The latter organometallic compound input port (C) also serves as a carrier gas discharge port, and there is a carrier gas discharge pipe (F) that bends from the top of the cylinder (^) to its circular periphery and then rises vertically. is connected to discharge a carrier gas containing saturated vapor of an organometallic compound via a cock (I). Then, the pipe (D) is connected via the cock (E).
The carrier gas is introduced into the cylinder (A) filled with the organometallic compound as shown by the arrow and reaches the bottom of the cylinder (A), during which time the vapor of the organometallic compound is released. The loaded carrier gas then passes through the disperser (H) and rises in the inner tube (G) also filled with the organometallic compound, as indicated by the arrow, where it is filled with the saturated vapor of the organometallic compound and passes through the exhaust pipe. via Road (F) to Kok (I)
).

このシリンダー(A)では、その下部(A1)は上部(
A2)に比べその内径を狭めた狭径部としであるが、こ
の狭径部(A1)の内径は内管(G)の直径の1.1倍
程度に設定しである。この狭径部の上には傾斜部(A3
)が続いて備えられ、この傾斜部(A3)は、シリンダ
ー上部(A2)に連続している。
In this cylinder (A), its lower part (A1) is the upper part (
This is a narrow diameter portion whose inner diameter is narrower than A2), and the inner diameter of this narrow diameter portion (A1) is set to about 1.1 times the diameter of the inner tube (G). Above this narrow diameter part is an inclined part (A3
) is subsequently provided, the slope (A3) continuing into the upper part of the cylinder (A2).

傾斜部(A3)の傾斜角度はO°〜50”の範囲で適宜
状められる。
The angle of inclination of the inclined portion (A3) is appropriately set within the range of 0° to 50''.

そこで第4図に示すようにこのシリンダー(A)(シリ
ンダー直径7511111.内管直径20IIII11
)および内管(G)の双方にTM I n57.9gを
充填(このうち15.3gは内管)し、20℃の恒温槽
(J)に浸は流量コントローラー(に)を設けた水素ガ
スライン(し)をキャリア−ガス導入管路(D)に接続
し、水素ガスを毎分500 mlで8時間連続的に導入
しTM I nのガスを排出させた。
Therefore, as shown in Fig. 4, this cylinder (A) (cylinder diameter 7511111, inner pipe diameter 20III11
) and the inner tube (G) were filled with 57.9 g of TM In (of which 15.3 g was in the inner tube), and the hydrogen gas was immersed in a constant temperature bath (J) at 20°C with a flow rate controller (in). The line (S) was connected to the carrier gas introduction conduit (D), and hydrogen gas was continuously introduced at a rate of 500 ml per minute for 8 hours to exhaust the TM I n gas.

水素ガス中のTMInlは、液体窒素トラップ(H)で
補集しその重量変化から測定した。測定後、再び水素ガ
スを同一流量、同一時間流しTMinの全使用量が充填
時の80%近くになるまでこの操作を繰り返した。測定
結果を第5図にボす。
TMInl in the hydrogen gas was collected with a liquid nitrogen trap (H) and measured from the change in weight. After the measurement, hydrogen gas was supplied again at the same flow rate and for the same period of time, and this operation was repeated until the total amount of TMin used reached nearly 80% of the filling amount. The measurement results are shown in Figure 5.

第5図の縦軸のTMIn供給!(g/Hr)とはTM 
I nとキャリア−ガスを接触させることにより得られ
るTMInのガス発生量を意味する。
TMIn supply on the vertical axis in Figure 5! (g/Hr) is TM
It means the amount of TMIn gas generated by bringing In into contact with a carrier gas.

〔従来例〕[Conventional example]

第3図に示すシリンダーを用い、TM I n57−2
gをシリンダー(2)内に充填し実施例に準じ水素ガス
を毎分500 mの割合で流した。水素ガス中のTM 
I nは実施例と同−法により補集し供給量の経時変化
を測定した。この場合、空洞の拡がりと共に供給量が低
下していった。結果を第5図に示す。
Using the cylinder shown in Figure 3, TM I n57-2
g was filled into the cylinder (2), and hydrogen gas was flowed at a rate of 500 m/min as in the example. TM in hydrogen gas
In was collected using the same method as in the example, and the change in supply amount over time was measured. In this case, the supply amount decreased as the cavity expanded. The results are shown in Figure 5.

(発明の効果) 本発明方法によれば、従来の方法と比較し、固体有機金
属化合物の充填量、キャリア−ガスの流量等に依存する
ことなく一定した有機金属化合物の供給量が長時間安定
して得られるので、単結晶薄膜の組成コントロールが可
能となりその工業的価値は大なるものがある。
(Effects of the Invention) According to the method of the present invention, compared to conventional methods, the supply amount of the organometallic compound is stable for a long time without depending on the filling amount of the solid organometallic compound, the flow rate of the carrier gas, etc. Therefore, it is possible to control the composition of single crystal thin films, which has great industrial value.

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

第1図は本発明方法に使用した有殿金属気相成長用シリ
ンダーの正面説明図、第2図は同シリンダーの平面説明
図、第3図は従来例のシリンダーの正面説明図、第4図
は第1図のシリンダーを組み込んだ試験装置の系統的説
明図、第5図は第4図の試験装置を用いて行った本発明
例のシリンダーおよび従来例のシリンダーの比較試験の
結果を示す図表である。 A シリンダー シリンダー下部(狭径部) シリンダー上部 傾斜部 有機金属化合物の投入管路 有機金属化合物の投入口 キャリア−ガスの導入管路 コック キャリア−ガスの排出管路 内管 分散器(フィルター) 圧力調節器 流量コントローラー 恒温槽 液体窒素トラップ 第2図 手続補正書 (自 発) 補正の内容 昭和63年8月23日
Fig. 1 is an explanatory front view of a cylinder for vapor phase growth of deposited metals used in the method of the present invention, Fig. 2 is an explanatory plan view of the same cylinder, Fig. 3 is an explanatory front view of a conventional cylinder, and Fig. 4 1 is a systematic explanatory diagram of a test device incorporating the cylinder shown in FIG. 1, and FIG. 5 is a chart showing the results of a comparative test between the cylinder of the present invention example and the cylinder of the conventional example conducted using the test device of FIG. 4. It is. A Cylinder Lower part of the cylinder (narrow diameter part) Slanted part of the upper part of the cylinder Organometallic compound inlet pipe Organometallic compound inlet Carrier - Gas inlet pipe Cock carrier - Gas discharge pipe Inner pipe Distributor (filter) Pressure adjustment Flow Controller Thermostat Liquid Nitrogen Trap Diagram 2 Procedure Amendment (Voluntary) Contents of Amendment August 23, 1988

Claims (2)

【特許請求の範囲】[Claims] (1)有機金属気相成長用シリンダーの上部に夫々キャ
リア−ガスの導入口および排出口を設け、この排出口に
直結しかつ底部に分散器を装備した内管を該シリンダー
内に挿入し、これらのシリンダーおよび内管内の双方に
有機金属化合物を夫々充填して前記導入口よりシリンダ
ー内に送入したキャリア−ガスをシリンダー内底部より
上記の分散器を経て内管を通り前記の排出口からシリン
ダー外に排出せしめることを特徴とする有機金属気相成
長法における有機金属化合物の飽和蒸気生成方法。
(1) An inlet and an outlet for carrier gas are provided at the top of a cylinder for organometallic vapor phase growth, and an inner tube directly connected to the outlet and equipped with a disperser at the bottom is inserted into the cylinder, Both the cylinder and the inner tube are filled with an organometallic compound, and the carrier gas is fed into the cylinder from the inlet port, from the bottom of the cylinder, through the above-mentioned disperser, through the inner tube, and from the outlet port. A method for generating saturated vapor of an organometallic compound in an organometallic vapor phase epitaxy method, which is characterized by discharging the vapor outside the cylinder.
(2)シリンダーがその下部を上部に比し内径を狭めた
形状のたて型円筒状であることを特徴とする有機金属気
相成長法における有機金属化合物の飽和蒸気生成方法。
(2) A method for generating saturated vapor of an organometallic compound in an organometallic vapor phase epitaxy method, characterized in that the cylinder has a vertical cylindrical shape with an inner diameter narrower at the lower part than at the upper part.
JP17489388A 1988-07-15 1988-07-15 Method of producing saturated vapor of organometal compound in organometallic vapor growth Granted JPH0226017A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17489388A JPH0226017A (en) 1988-07-15 1988-07-15 Method of producing saturated vapor of organometal compound in organometallic vapor growth

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17489388A JPH0226017A (en) 1988-07-15 1988-07-15 Method of producing saturated vapor of organometal compound in organometallic vapor growth

Publications (2)

Publication Number Publication Date
JPH0226017A true JPH0226017A (en) 1990-01-29
JPH0531293B2 JPH0531293B2 (en) 1993-05-12

Family

ID=15986527

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17489388A Granted JPH0226017A (en) 1988-07-15 1988-07-15 Method of producing saturated vapor of organometal compound in organometallic vapor growth

Country Status (1)

Country Link
JP (1) JPH0226017A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06154579A (en) * 1992-11-26 1994-06-03 Japan Atom Energy Res Inst Raw material container

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06154579A (en) * 1992-11-26 1994-06-03 Japan Atom Energy Res Inst Raw material container

Also Published As

Publication number Publication date
JPH0531293B2 (en) 1993-05-12

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