JP2525009B2 - Vapor phase growth equipment - Google Patents
Vapor phase growth equipmentInfo
- Publication number
- JP2525009B2 JP2525009B2 JP62179889A JP17988987A JP2525009B2 JP 2525009 B2 JP2525009 B2 JP 2525009B2 JP 62179889 A JP62179889 A JP 62179889A JP 17988987 A JP17988987 A JP 17988987A JP 2525009 B2 JP2525009 B2 JP 2525009B2
- Authority
- JP
- Japan
- Prior art keywords
- container
- diameter portion
- vapor phase
- susceptor
- phase growth
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、サセプタ上のウエハ表面に半導体薄膜を気
相成長させる気相成長装置に関するものである。Description: TECHNICAL FIELD The present invention relates to a vapor phase growth apparatus for performing vapor phase growth of a semiconductor thin film on a wafer surface on a susceptor.
[従来技術] 従来のこの主の有機金属化学堆積法(以下MOCVD法と
いう。)の気相成長装置は、第8図に示すように、シャ
フト1に支持されたサセプタ2を容器3内に置き、また
容器3内にはサセプタ2が置かれた位置に対応してサセ
プタ2を包囲する内管4を置き、容器3内に気相成長用
ガスを入口5から供給して一方向に流すことによりサセ
プタ2上のウエハ6の表面に半導体薄膜を結晶成長さ
せ、排ガスは容器3の他端寄りの出口7から排出させる
構造であった。なお、8はサセプタ2や内管4の出し入
れのための容器3の開口部3Eを閉塞する蓋である。[Prior Art] A conventional vapor phase growth apparatus of this metalorganic chemical vapor deposition method (hereinafter referred to as MOCVD method) has a susceptor 2 supported by a shaft 1 placed in a container 3 as shown in FIG. In addition, an inner tube 4 surrounding the susceptor 2 is placed in the container 3 at a position corresponding to the position where the susceptor 2 is placed, and gas for vapor phase growth is supplied from the inlet 5 into the container 3 to flow in one direction. Thus, the semiconductor thin film is crystal-grown on the surface of the wafer 6 on the susceptor 2, and the exhaust gas is discharged from the outlet 7 near the other end of the container 3. Reference numeral 8 is a lid that closes the opening 3E of the container 3 for inserting and removing the susceptor 2 and the inner tube 4.
この場合、内管4は反応生成物が容器3の内壁に付着
・堆積するのを防止し、且つその反応生成物を容器3の
外に除去するのを容易にするために設けられている。In this case, the inner pipe 4 is provided to prevent the reaction product from adhering to and depositing on the inner wall of the container 3 and to facilitate the removal of the reaction product outside the container 3.
しかしながら、このような構造では、内管4と容器3
との間に隙間9が存在し、該隙間9が上流側に開口して
いるので、該隙間9に気相成長用ガスが入り込み、容器
3の内壁に反応生成物が付着・堆積するという問題点が
あった。However, in such a structure, the inner tube 4 and the container 3 are
Since there is a gap 9 between the gap 9 and the gap 9, and the gap 9 is open to the upstream side, the gas for vapor phase growth enters the gap 9 and the reaction product adheres to and deposits on the inner wall of the container 3. There was a point.
これを解決するために、第9図に示すように、内管3
の上流側端部に隣接した位置の容器3の部分に段差部3A
を設け、該容器3を段差部3Aより上流側が小径部3B、段
差部3Aより下流側が大径部3Cとなるようにし、大径部3C
内には段差部3Aに一端を位置させて補助管10を設け、該
補助管10の内側を容器3の小径部3Bの内径にほぼ一致さ
せた構造の気相成長装置も提案されている。このような
気相成長装置では、段差部3Aに一端を位置させた補助管
10の存在により、反応生成物が容器3の内壁に付着・堆
積するのを防止できる。In order to solve this, as shown in FIG.
3A on the portion of the container 3 adjacent to the upstream end of the
Is provided so that the upstream side of the stepped portion 3A is the small diameter portion 3B and the downstream side of the stepped portion 3A is the large diameter portion 3C.
There is also proposed a vapor phase growth apparatus having a structure in which one end of the auxiliary pipe 10 is provided in the stepped portion 3A, and the inside of the auxiliary pipe 10 is substantially matched with the inner diameter of the small diameter portion 3B of the container 3. In such a vapor phase growth apparatus, an auxiliary tube whose one end is located at the step 3A
The presence of 10 can prevent the reaction product from adhering to and depositing on the inner wall of the container 3.
[発明が解決しようとする問題点] しかしながら、このような気相成長装置では、容器3
内に内管4と補助管10とを収容しなければならないの
で、構造が複雑になり、また内管4の交換に時間がかか
る問題点があった。また、このような構造では、容器3
内には内管4が突出しているので、容器3内を流れるガ
ス流が乱れ、ウエハ6上の膜厚を均一に成長させにくい
問題点があった。[Problems to be Solved by the Invention] However, in such a vapor phase growth apparatus, the container 3
Since the inner tube 4 and the auxiliary tube 10 must be housed inside, the structure is complicated and it takes time to replace the inner tube 4. Further, in such a structure, the container 3
Since the inner tube 4 projects inside, the gas flow flowing in the container 3 is disturbed, and there is a problem that it is difficult to uniformly grow the film thickness on the wafer 6.
本発明の目的は、容器内に内管を収容してもガス流の
乱れを防止でき、しかも構造が簡単な気相成長装置を提
供することにある。It is an object of the present invention to provide a vapor phase growth apparatus that can prevent turbulence of a gas flow even if an inner tube is housed in a container and has a simple structure.
[問題点を解決するための手段] 上記の目的を達成するための本発明の構成を説明する
と、本発明はシャフトに支持されたサセプタを容器内に
置き、また前記容器内には前記サセプタが置かれる位置
に対応して前記サセプタを包囲する内管を置き、前記容
器内に気相成長用ガスを一方向に流して前記サセプタ上
のウエハの表面に結晶成長させる気相成長装置におい
て、前記容器はその途中の段差部が境にしてそれより上
流側が小径部、下流側が大径部として形成され、且つ前
記小径部には前記段差部より前記大径部内に突出する延
長部が設けられ、前記内管は前記延長部の外周に一端を
嵌合して前記大径部内に配設されていることを特徴とす
る。[Means for Solving the Problems] To explain the configuration of the present invention for achieving the above object, the present invention places a susceptor supported by a shaft in a container, and the susceptor is provided in the container. An inner tube surrounding the susceptor is placed corresponding to a position to be placed, and a gas for vapor phase growth is caused to flow in one direction in the container to cause crystal growth on a surface of a wafer on the susceptor, The container is formed with a small-diameter portion on the upstream side and a large-diameter portion on the downstream side with the step portion in the middle as a boundary, and the small-diameter portion is provided with an extension portion projecting from the step portion into the large-diameter portion, The inner pipe is arranged in the large-diameter portion with one end fitted to the outer periphery of the extension portion.
[作用] このように、大径部内に突出した小径部の延長部に内
管の一端を嵌合して内管を大径部内に配置すると、内管
が容器内に突出しなくなり、ガスの流れを乱さなくな
り、ウエハの表面欠陥を減少させることができる。ま
た、容器内には補助管を更にセットする必要がなくな
り、構造が簡単になる。更に、延長部の存在により内管
の位置決めも容易になる。[Operation] As described above, when one end of the inner pipe is fitted to the extension portion of the small diameter portion protruding into the large diameter portion and the inner pipe is arranged in the large diameter portion, the inner pipe does not protrude into the container and the gas flow is prevented. The surface defects of the wafer can be reduced. Further, it is not necessary to further set an auxiliary pipe in the container, which simplifies the structure. Furthermore, the presence of the extension facilitates positioning of the inner tube.
[実施例] 以下、本発明の実施例を図面を参照して詳細に説明す
る。第1図乃至第5図は、横型タイプの化学輸送法(以
下、CVT法)による気相成長装置に本発明を適用した例
を示したものである。なお、前述した第8図及び第9図
に対応した部分には同一符号をつけて示している。本実
施例においても、断面円形の容器3はその途中の段差部
3Aを中心とした上流側が小径部3B、下流側が大径部3Cと
して形成され、且つ小径部3Bには段差部3Aより大径部3C
内に突出する延長部3Dが小径部3Bと同じ内径で設けられ
ている。この場合、小径部3B及び延長部3Dの内径は例え
ば40mmφ、大径部3Cの内径は例えば54mmφ、延長部3Dの
長さは約20mmである。Embodiments Embodiments of the present invention will be described in detail below with reference to the drawings. 1 to 5 show an example in which the present invention is applied to a vapor phase growth apparatus by a lateral type chemical transport method (hereinafter, CVT method). The parts corresponding to those in FIGS. 8 and 9 described above are designated by the same reference numerals. Also in this embodiment, the container 3 having a circular cross section has a stepped portion in the middle thereof.
The small diameter portion 3B is formed on the upstream side of 3A and the large diameter portion 3C is formed on the downstream side, and the small diameter portion 3B has a larger diameter portion 3C than the step portion 3A.
An extension portion 3D protruding inward is provided with the same inner diameter as the small diameter portion 3B. In this case, the inner diameter of the small diameter portion 3B and the extension portion 3D is, for example, 40 mmφ, the inner diameter of the large diameter portion 3C is, for example, 54 mmφ, and the length of the extension portion 3D is about 20 mm.
本実施例における内管4は、容器3の延長部3Dの外径
とほぼ等しい内径をもつ円筒部4Aと、この円筒部4Aの断
面円形から断面四角形に徐々に変化するテーパ部4Bと、
このテーパ部4Bの断面四角形の端部に連続する断面四角
形の四角筒部4Cとで構成されている。このような内管4
は、円筒部4Aを延長部3Dの外周に挿入し容器3の大径部
3C内に配設されている。この場合、円筒部4Aの内径は例
えば延長部3Dの外径より1mm大きい47mmφ、四角筒部4C
の孔の幅は例えば47mm、高さは30mmである。The inner pipe 4 in this embodiment has a cylindrical portion 4A having an inner diameter substantially equal to the outer diameter of the extension 3D of the container 3, and a tapered portion 4B gradually changing from a circular cross section of the cylindrical portion 4A to a square cross section.
The tapered portion 4B is composed of a square tubular portion 4C having a quadrangular cross section that is continuous with an end portion of the quadrangular cross section. Inner tube 4 like this
Is a large diameter part of the container 3 with the cylindrical part 4A inserted into the outer periphery of the extension part 3D.
It is located in 3C. In this case, the inner diameter of the cylindrical portion 4A is, for example, 47 mmφ which is 1 mm larger than the outer diameter of the extension portion 3D, and the square tubular portion 4C.
The hole has a width of 47 mm and a height of 30 mm, for example.
また、容器3の小径部3B内にはボート11が配置され、
該ボート11上には固体ガリウムGaソース12が載置されて
いる。Further, the boat 11 is arranged in the small diameter portion 3B of the container 3,
A solid gallium Ga source 12 is placed on the boat 11.
次に、このような装置でウエハ6上にGaAsを結晶成長
させる例について説明する。まず、容器3内に内管4を
挿入し、気相エッチングを行う。この気相エッチングの
終了後に内管4を新しいものと交換し、Gaソース12をボ
ート11で容器3内の所定位置に挿入し、容器3の外部の
図示しないヒータでGaソース12を約850℃まで加熱す
る。このとき、AsCl3とキャリアガス(H2)を容器3内
に入口5から供給し、Ga融液中にAsを溶解させる。この
とき生成されるGaの塩化物や小量のAs,GaAs等は内管4
に堆積し、この工程が終了後に内管4を交換する。次に
容器3内にサセプタ2を介してGaAsウエハ6を挿入し、
ウエハ6及びGaソース12をそれぞれ所定温度(ウエハ:7
00〜750℃、Gaソース850℃)に昇温させ、AsCl3とキャ
リアガス(H2)を内管4内に入口5から供給して、GaAs
ウエハ6上にエピタキシャル成長させる。このとき、生
成されたGaの塩化物,As,GaAsが内管4に堆積する。この
内管4を交換し、ヒータを切り、ウエハ6の冷却を行
う。Next, an example of crystal-growing GaAs on the wafer 6 with such an apparatus will be described. First, the inner tube 4 is inserted into the container 3 and vapor phase etching is performed. After completion of this vapor phase etching, the inner tube 4 is replaced with a new one, the Ga source 12 is inserted into the container 3 at a predetermined position by the boat 11, and the Ga source 12 is heated to about 850 ° C. by a heater (not shown) outside the container 3. Heat up to. At this time, AsCl 3 and carrier gas (H 2 ) are supplied into the container 3 from the inlet 5 to dissolve As in the Ga melt. The chloride of Ga and small amounts of As, GaAs, etc. generated at this time are in the inner tube 4
And the inner tube 4 is replaced after this step is completed. Next, insert the GaAs wafer 6 into the container 3 via the susceptor 2,
The wafer 6 and the Ga source 12 are heated to a predetermined temperature (wafer: 7
The temperature is raised to 00-750 ° C, Ga source 850 ° C), AsCl 3 and carrier gas (H 2 ) are supplied into the inner tube 4 from the inlet 5, and GaAs is supplied.
Epitaxial growth is performed on the wafer 6. At this time, the generated Ga chloride, As, and GaAs are deposited on the inner tube 4. The inner tube 4 is replaced, the heater is turned off, and the wafer 6 is cooled.
従来の装置と比較して本発明の装置を用いた製造方法
によれば、ウエハ表面の欠陥数が10〜20%減少し、結晶
膜厚の均一性やその再現性も良くなった。According to the manufacturing method using the apparatus of the present invention as compared with the conventional apparatus, the number of defects on the wafer surface was reduced by 10 to 20%, and the uniformity of the crystal film thickness and its reproducibility were improved.
代表的な成長条件 キャリアガス流量H2:1000cc/min AsCl3バプリング流量H2:300cc/min Gaソース温度 :850℃ ウエハ温度 :730℃ ウエハ寸法 :30mm×20mm ウエハ枚数 :2枚 なお、第1図乃至第5図の装置は、ボート11に乗せて
Gaソース12を供給する代りに、入口5から原料ガスも供
給するMOCVD法にも適用できることは勿論である。Typical growth conditions Carrier gas flow rate H 2 : 1000cc / min AsCl 3 bubbling flow rate H 2 : 300cc / min Ga source temperature: 850 ℃ Wafer temperature: 730 ℃ Wafer size: 30mm × 20mm Number of wafers: 2 The device shown in Figs.
Of course, instead of supplying the Ga source 12, the MOCVD method of supplying the source gas from the inlet 5 can also be applied.
第6図及び第7図は縦型タイプのMOCVD法による気相
成長装置に本発明を提供した例を示したものである。こ
の実施例では、容器3は上下に配置されたリアクタ13と
プリチャンバ14とで構成されている。リアクタ13の箇所
で容器3は前述したと同様に段差部3Aを中心とした上流
側が小径部3B、下流側が大径部3Cとして形成され、且つ
小径部3Bには段差部3Aより大径部3C内に突出する延長部
3Dが該小径部3Bと等しい内径で設けられている。例え
ば、小径部3B及び延長部3Dの内径は140mmφ、大径部3C
の内径は156mmφである。延長部3Dに一端を嵌合して大
径部3C内には内管4が配置されている。内管4は延長部
3Dに嵌合される部分の内径が該延長部3Dの外径とほぼ等
しく例えば146mmφに形成され、その他の部分は延長部3
Dの内径とほぼ等しく形成されている。内管4は内管昇
降台15上に搭載され、該内管昇降台15は内管昇降軸16で
昇降されるようになっている。内管4には容器3の出口
7に対応して排気口17が形成されている。段差部3Aに連
続した容器3の大径部3Cの外周には冷却ジャケット18が
液密に取り付けられ、その外周には加熱用の誘導加熱コ
イル等の加熱手段19が配設されている。内管4の下に対
応して容器3にはゲートバルブ20が設けられ、容器3内
の上下の仕切り閉鎖が行えるようになっている。容器3
のプリチャンバ14の部分には開閉用扉21が設けられてい
る。プリンチャンバ14の下端には各軸1,16のシール部2
2,23が設けられている。FIGS. 6 and 7 show an example in which the present invention is applied to a vapor phase growth apparatus by a vertical type MOCVD method. In this embodiment, the container 3 is composed of a reactor 13 and a pre-chamber 14 arranged one above the other. At the location of the reactor 13, the container 3 is formed with a small diameter portion 3B on the upstream side and a large diameter portion 3C on the downstream side centering on the stepped portion 3A, and the small diameter portion 3B has a larger diameter portion 3C than the stepped portion 3A as described above. Extension that projects inward
3D is provided with an inner diameter equal to that of the small diameter portion 3B. For example, the inner diameter of the small diameter part 3B and the extension part 3D is 140mmφ, the large diameter part 3C
The inner diameter of is 156 mmφ. One end is fitted to the extension portion 3D and the inner pipe 4 is arranged in the large diameter portion 3C. Inner tube 4 is an extension
The inner diameter of the portion to be fitted to the 3D is approximately equal to the outer diameter of the extension portion 3D, and is formed to be 146 mmφ, for example, and the other portion is extended 3
It is formed to have a diameter almost equal to that of D. The inner pipe 4 is mounted on an inner pipe lift base 15, and the inner pipe lift base 15 is moved up and down by an inner pipe lift shaft 16. An exhaust port 17 is formed in the inner pipe 4 corresponding to the outlet 7 of the container 3. A cooling jacket 18 is liquid-tightly attached to the outer periphery of the large diameter portion 3C of the container 3 continuous with the step portion 3A, and a heating means 19 such as an induction heating coil for heating is disposed on the outer periphery thereof. A gate valve 20 is provided in the container 3 under the inner pipe 4 so that upper and lower partitions in the container 3 can be closed. Container 3
An opening / closing door 21 is provided in the pre-chamber 14 part. At the lower end of the purine chamber 14, there is a seal part 2 for each shaft 1, 16.
2,23 are provided.
このような装置においては、まずゲートバルブ20を占
め、プリチャンバ14の扉21を開いて内管4を内管昇降台
15上に設置し、扉21を閉め、プリチャンバ14をH2等の置
換ガスでパージする。パージ後、ゲートバルブ20を開
き、まずサセプタ2を所定位置まで上昇させ、次に内管
4を内管昇降台15と共に所定の位置まで上昇させる。内
管4が上昇された状態では、内管4の段差部4Aが延長部
3Dの端部に当接され、隙間ができないようになる。膜厚
を均一にするため、サセプタ2をシャフト1を介して回
転させつつリアクタ13内に入口5からキャリアガス
(H2)を供給し、サセプタ2上のウエハ6を加熱手段20
により加熱し、その温度が300℃に達した時点で入口5
から気相成長用のガスであるアルシン(AsH3)を流し、
ウエハ6の温度が700℃に安定してから、入口5からト
リメチルガリウム(TMG)を流し、GaAs結晶をウエハ6
上に成長させる。成長作業中に、GaAsやAsが内管4の表
面にかなりつくが、リアクタ13にほとんどつかない。成
長が終了すると、加熱を止め、ウエハ6の温度が400℃
になったところでAsH3の供給を停止する。ウエハ6の温
度が100〜200℃まで下がったところで、パージガスの供
給を停止し、ゲートバルブ20を開け、内管4を内管昇降
台15と共に下げ、次にサセプタ2を下げる。下げが終わ
ると、ゲートバルブ20を閉じ、N2ガスでプリチャンバ14
内をパージする。パージ終了後、プリチャンバ14の扉21
を開け、内管4を取り出し、次にウエハ6を取り出し、
新しいウエハ6をサセプタ2にセットし、次に新しい内
管4を内管昇降台15上にセットし、次の成長作業に入
る。In such a device, first, the gate valve 20 is occupied, the door 21 of the pre-chamber 14 is opened, and the inner pipe 4 is moved up and down.
Installed on top of the above, closed the door 21, and purged the pre-chamber 14 with a replacement gas such as H 2 . After purging, the gate valve 20 is opened, the susceptor 2 is first raised to a predetermined position, and then the inner pipe 4 is raised to a predetermined position together with the inner pipe lifting table 15. When the inner pipe 4 is raised, the step portion 4A of the inner pipe 4 extends
It comes into contact with the 3D end, and no gap is created. In order to make the film thickness uniform, the carrier gas (H 2 ) is supplied from the inlet 5 into the reactor 13 while rotating the susceptor 2 via the shaft 1, and the wafer 6 on the susceptor 2 is heated by the heating means 20.
When the temperature reaches 300 ° C, the inlet 5
Arsine (AsH 3 ) which is a gas for vapor phase growth is flowed from
After the temperature of the wafer 6 stabilizes at 700 ° C., trimethylgallium (TMG) is flown from the inlet 5 to remove the GaAs crystal from the wafer 6.
Grow on. During the growth operation, GaAs and As are considerably attached to the surface of the inner tube 4, but are hardly attached to the reactor 13. When the growth is completed, the heating is stopped and the temperature of the wafer 6 is 400 ° C.
When that happens, the supply of AsH 3 is stopped. When the temperature of the wafer 6 has dropped to 100 to 200 ° C., the supply of the purge gas is stopped, the gate valve 20 is opened, the inner pipe 4 is lowered together with the inner pipe lifting table 15, and then the susceptor 2 is lowered. When the lowering is complete, close the gate valve 20 and pre-chamber 14 with N 2 gas.
Purge the inside. After purging, the pre-chamber 14 door 21
Open, take out the inner tube 4, then take out the wafer 6,
A new wafer 6 is set on the susceptor 2, then a new inner tube 4 is set on the inner tube lift 15 to start the next growth operation.
代表的な成長条件 キャリアガス流量H2:100/min V族原料ガス流量AsH3:160cc/min III族バブリングガスH2:100cc/min ウエハ温度 :700℃ サセプタ形状 :六角錐台 ウエハ枚数 :6枚 このようにして成長させたウエハ6の表面欠陥は、従
来が500個/cm2であったのに対し、この発明では100〜20
0個/cm2と減少した。また、容器3への反応生成物の付
着もほとんどなくなり、リアクタ13への反応生成物の付
着もほとんど無くなり、リクアタ13の交換頻度を激減さ
せることができた。Typical growth conditions Carrier gas flow rate H 2 : 100 / min Group V source gas flow rate AsH 3 : 160cc / min Group III bubbling gas H 2 : 100cc / min Wafer temperature: 700 ℃ Susceptor shape: Hexagonal pyramid Number of wafers: 6 The number of surface defects of the wafer 6 thus grown was 500 / cm 2 in the conventional case, but 100 to 20 in the present invention.
The number decreased to 0 / cm 2 . In addition, the reaction product adhered to the container 3 almost disappeared, and the reaction product adhered to the reactor 13 almost disappeared, so that the replacement frequency of the liquor 13 could be drastically reduced.
[発明の効果] 以上説明したように本発明では、容器の途中に段差部
を設け、この段差部を境にして上流側を小径部、下流側
を大径部とし、且つ小径部には段差部より大径部内に突
出する延長部を設け、この延長部の外周に一端を嵌合さ
せて内管を大径部内に設けたので、内管が容器内に突出
しなくなり、ガスの流れを乱さなくなり、ウエハの表面
欠陥を減少させることができる。更に、本発明によれ
ば、容器への反応生成物の付着堆積が非常に少なくな
り、容器の交換頻度を著しく減少させることができる。
また、本発明では、内管以外の補助管等を入れなくて良
いので、構造が簡単になり、且つ交換時の取扱いが容易
となる利点がある。更に、本発明では、内管を延長部を
嵌合しているので、内管の位置決めが容易になり、且つ
使用中のずれも防止できる利点がある。[Effects of the Invention] As described above, according to the present invention, a step portion is provided in the middle of a container, and a small diameter portion is provided on the upstream side and a large diameter portion is provided on the downstream side with the step portion as a boundary, and a step is provided on the small diameter portion. Since an extension part is provided that protrudes into the larger diameter part than the other part and one end is fitted to the outer circumference of this extension part and the inner pipe is provided inside the large diameter part, the inner pipe does not protrude into the container and disturbs the gas flow. The surface defects of the wafer can be reduced. Further, according to the present invention, the deposition and deposition of the reaction product on the container can be significantly reduced, and the frequency of container replacement can be significantly reduced.
Further, in the present invention, since it is not necessary to insert auxiliary pipes other than the inner pipe, there is an advantage that the structure is simple and handling at the time of replacement is easy. Further, in the present invention, since the extension portion is fitted to the inner tube, there is an advantage that the positioning of the inner tube is facilitated and the shift during use can be prevented.
第1図は本発明に係る装置の第1実施例の概略構成を示
す縦断面図、第2図は第1図の要部拡大縦断面図、第3
図は第1実施例で使用している内管の縦断面図、第4図
は第3図のX−X線断面図、第5図は第3図のY−Y線
断面図、第6図は本発明に係る装置の第2実施例の縦断
面図、第7図は第6図の要部拡大縦断面図、第8図及び
第9図は従来の装置の2種の例を示す縦断面図である。 1……シャフト、2……サセプタ、3……容器、3A……
段差部、3B……小径部、33C……大径部、3D……延長
部、4……内管、5……入口、6……ウエハ、7……出
口。1 is a vertical sectional view showing a schematic configuration of a first embodiment of an apparatus according to the present invention, FIG. 2 is an enlarged vertical sectional view of an essential part of FIG. 1, and FIG.
FIG. 4 is a longitudinal sectional view of the inner pipe used in the first embodiment, FIG. 4 is a sectional view taken along line XX of FIG. 3, and FIG. 5 is a sectional view taken along line YY of FIG. FIG. 8 is a vertical cross-sectional view of a second embodiment of the device according to the present invention, FIG. 7 is an enlarged vertical cross-sectional view of an essential part of FIG. 6, and FIGS. 8 and 9 show two examples of conventional devices. FIG. 1 ... Shaft, 2 ... Susceptor, 3 ... Container, 3A ...
Step portion, 3B ... small diameter portion, 33C ... large diameter portion, 3D ... extension portion, 4 ... inner tube, 5 ... inlet, 6 ... wafer, 7 ... exit.
Claims (1)
置き、また前記容器内には前記サセプタが置かれる位置
に対応して前記サセプタを包囲する内管を置き、前記容
器内に気相成長用ガスを一方向に流して前記サセプタ上
のウエハの表面に結晶成長させる気相成長装置におい
て、前記容器はその途中の段差部を境にしてそれより上
流側が小径部、下流側が大径部として形成され、且つ前
記小径部には前記段差部より前記大径部内に突出する延
長部が設けられ、前記内管は前記延長部の外周に一端を
嵌合して前記大径部内に配設されていることを特徴とす
る気相成長装置。1. A susceptor supported by a shaft is placed in a container, and an inner tube surrounding the susceptor is placed in the container at a position where the susceptor is placed, and vapor phase growth is carried out in the container. In a vapor phase growth apparatus for flowing a working gas in one direction to grow crystals on the surface of a wafer on the susceptor, the container has a small diameter portion on the upstream side and a large diameter portion on the downstream side with a step portion in the middle as a boundary. An extension portion is formed in the small diameter portion and protrudes into the large diameter portion from the step portion, and the inner pipe is disposed in the large diameter portion by fitting one end to an outer periphery of the extension portion. A vapor phase growth apparatus characterized in that
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62179889A JP2525009B2 (en) | 1987-07-21 | 1987-07-21 | Vapor phase growth equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62179889A JP2525009B2 (en) | 1987-07-21 | 1987-07-21 | Vapor phase growth equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6424414A JPS6424414A (en) | 1989-01-26 |
| JP2525009B2 true JP2525009B2 (en) | 1996-08-14 |
Family
ID=16073669
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62179889A Expired - Fee Related JP2525009B2 (en) | 1987-07-21 | 1987-07-21 | Vapor phase growth equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2525009B2 (en) |
-
1987
- 1987-07-21 JP JP62179889A patent/JP2525009B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6424414A (en) | 1989-01-26 |
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