JP3076268B2 - Low pressure vapor phase growth equipment - Google Patents
Low pressure vapor phase growth equipmentInfo
- Publication number
- JP3076268B2 JP3076268B2 JP09160091A JP16009197A JP3076268B2 JP 3076268 B2 JP3076268 B2 JP 3076268B2 JP 09160091 A JP09160091 A JP 09160091A JP 16009197 A JP16009197 A JP 16009197A JP 3076268 B2 JP3076268 B2 JP 3076268B2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- pressure vapor
- boat
- vapor phase
- furnace core
- 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 - Lifetime
Links
Description
【0001】[0001]
【発明の属する技術分野】本発明は、半導体製造措置に
関わり、特に、半導体基板(ウエハ)に原料ガスに応じ
た膜を気相成長させる減圧気相成長装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a semiconductor manufacturing process, and more particularly to a reduced pressure vapor phase growth apparatus for vapor phase growing a film on a semiconductor substrate (wafer) according to a source gas.
【0002】[0002]
【従来の技術】従来より、半導体の製造においては、電
極形成やマスクを用いた膜形成等、多くの成膜工程があ
り、減圧気相成長装置が用いられている。図2は、従来
の縦型減圧気相成長装置の断面図である。2. Description of the Related Art Conventionally, in the manufacture of semiconductors, there have been many film forming steps such as electrode formation and film formation using a mask, and a reduced-pressure vapor deposition apparatus has been used. FIG. 2 is a cross-sectional view of a conventional vertical reduced pressure vapor deposition apparatus.
【0003】図2の縦型減圧気相成長装置は、炉芯管1
と、炉芯管1内を所望の温度に保つためのヒータ2と、
ウエハ3を搭載するボート4と、炉芯管1内を減圧状態
にし、反応ガスの排気を行なうポンプ5と、炉芯管1の
密閉を行なうハッチ6と、炉芯管1の内部に原料ガスを
導入するガス導入管7と、導入した原料ガスを二分して
一部を排気側に近い反応部へ流すようにした二重管構造
の外側内管9及び内側内管10を有している。外側内管
9は、内側内管10よりも長く形成されている。[0003] The vertical type reduced pressure vapor deposition apparatus shown in FIG .
A heater 2 for keeping the inside of the furnace core tube 1 at a desired temperature;
A boat 4 on which the wafer 3 is mounted, a pump 5 for depressurizing the inside of the furnace core tube 1 and exhausting the reaction gas, a hatch 6 for sealing the furnace core tube 1, and a raw material gas inside the furnace core tube 1. And an inner inner tube 9 having a double tube structure in which the introduced raw material gas is divided into two and a part of the gas flows into a reaction section near the exhaust side. . The outer inner tube 9 is formed longer than the inner inner tube 10.
【0004】従来の、縦型減圧気相成長装置におけるウ
エハ上への所望の成膜は、以下のように行う。まず、ヒ
ータ2により所望の温度に保たれた炉芯管1内に、ウエ
ハ3を搭載したボート4を挿入し、ハッチ6により炉芯
管1を密閉し、ポンプ5により炉芯管1内を所望の圧力
に減圧し、その後、原料ガスを導入管7より供給し、ガ
ス濃度が低下する排気側に位置するウエハ3上には、外
側内管9と内側内管10との間隙を通った比較的高濃度
の原料ガスを導入して成膜を行う。未反応の原料ガス
は、ポンプ5により排気され、炉芯管1外へ排出される
ようになっている。A desired film formation on a wafer in a conventional vertical type reduced pressure vapor phase epitaxy apparatus is performed as follows. First, the boat 4 on which the wafer 3 is mounted is inserted into the furnace core tube 1 kept at a desired temperature by the heater 2, the furnace core tube 1 is sealed by the hatch 6, and the inside of the furnace core tube 1 is After reducing the pressure to a desired pressure, the raw material gas was supplied from the introduction pipe 7, and passed through the gap between the outer inner pipe 9 and the inner inner pipe 10 on the wafer 3 located on the exhaust side where the gas concentration was reduced. A film is formed by introducing a relatively high-concentration source gas. Unreacted raw material gas is exhausted by the pump 5 and discharged to the outside of the furnace core tube 1.
【0005】[0005]
【0006】[0006]
【0007】[0007]
【0008】[0008]
【発明が解決しようとする課題】 しかし、この図2の装
置では、内側内管10がとぎれる部分から、内管は二重
管ではなくなり外側内管9のみとなるため、内管径が急
激に拡大し、炉芯管1の内圧が下がるという傾向があ
る。このため、内側内管10がとぎれる部分での原料ガ
スの分圧が下がり、膜厚あるいは不純物濃度が低下する
という問題があった。However, in the apparatus shown in FIG. 2, the inner pipe is not a double pipe but only the outer inner pipe 9 from the portion where the inner inner pipe 10 is cut off . There is a tendency that the pressure increases and the internal pressure of the furnace core tube 1 decreases. For this reason, there is a problem that the partial pressure of the raw material gas at the portion where the inner inner pipe 10 is cut off decreases, and the film thickness or the impurity concentration decreases.
【0009】本発明は、同一バッチ内のウエハ上に成膜
される膜厚や不純物濃度、または膜質構造を均一にし、
製品での製造ばらつきを低減することを目的とする。According to the present invention, the film thickness, impurity concentration, or film quality structure formed on wafers in the same batch is made uniform,
The purpose is to reduce manufacturing variations in products.
【0010】[0010]
【課題を解決するための手段】本発明は、ウエハを搭載
したボートを炉芯管内に装填し、ボートと炉芯管との間
にボートを囲む二重管構造の内管を設置し、炉芯管内を
減圧するとともに、反応ガスを二重管の外側内管と内側
内管との間及び内側内管の内側に導入してウエハに膜成
長を行う減圧気相成長装置において、前記二重管の外側
内管を延長し、延長部をテーパ状に絞り込んでその先を
細くし、内管は一端側が二重管構造であり、他端側が単
管構造であることを特徴とする減圧気相成長装置であ
る。According to the present invention, a boat on which wafers are mounted is loaded into a furnace core tube, and an inner tube having a double tube structure surrounding the boat is installed between the boat and the furnace core tube. Depressurize the inside of the core tube and transfer the reaction gas to the inner and outer tubes of the double tube.
In a reduced pressure vapor phase epitaxy apparatus for growing a film on a wafer by introducing a film between the inner tube and the inner side of the inner tube, the outer inner tube of the double tube is extended, and the extended portion is narrowed down to a tapered shape. , And the inner tube has a double-tube structure at one end and a single-tube structure at the other end.
【0011】[0011]
【発明の実施の形態】次に、本発明の実施の形態を図面
を用いて説明する。図1は本発明の実施の形態を示す縦
型減圧気相成長装置の断面図であり、成長する膜をin
−situPドープSiを例にとって説明する。Next, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a cross-sectional view of a vertical type reduced pressure vapor phase epitaxy apparatus showing an embodiment of the present invention.
The description will be made by taking -situP-doped Si as an example.
【0012】反応管となる炉芯管1と、炉芯管1内を所
望の温度(例えば500〜550℃)に保つためのヒー
タ2と、ウエハ3を搭載するボート4と、炉芯管1内を
減圧状態、例えば0.5〜5Torrまでにガスの排気
を行うポンプ5と、炉芯管1の密閉を行うハッチ6と、
炉芯管1の内部に原料ガス、例えばSiH4とPH3を
導入するガス導入管7と、排気側で反応により低下した
原料ガス、例えばPH3を補うための補充ガス導入管8
と、これら原料ガスを、反応を押さえながら排気側反応
部へ導入する外側内管9a及び内側内管10からなる二
重管構造を有している。A furnace core tube 1 serving as a reaction tube, a heater 2 for maintaining the inside of the furnace core tube 1 at a desired temperature (for example, 500 to 550 ° C.), a boat 4 on which a wafer 3 is mounted, and a furnace core tube 1 A pump 5 for evacuating the gas to a reduced pressure state, for example, 0.5 to 5 Torr, a hatch 6 for sealing the furnace tube 1,
A gas introducing pipe 7 for introducing a raw material gas, for example, SiH4 and PH3, into the furnace core tube 1, and a replenishing gas introducing pipe 8 for supplementing the raw material gas, for example, PH3, which has been reduced by the reaction on the exhaust side.
And a double pipe structure comprising an outer inner pipe 9a and an inner inner pipe 10 for introducing these source gases into the exhaust-side reaction section while suppressing the reaction.
【0013】この外側内管9aは、上部を内側内管10
よりも延長し、延長部は内側内管10と同一の内径とな
るように、上部の管径をテーパ状に絞って細くし、単管
構造としてある。細くした部分の内径は、内側内管10
の内径と等しくする。また、外側内管9aと内側内管1
0との隙間は、外側内管9aと内側内管10との間に逆
拡散が起きない程度であればよく、例えば、300mm
の内側内管内径に対し、50mm程度でよい。また、内
側内管10の長さは、ボート4の中程までとし、外側内
管9aの長さは、ボート4の頂部よりやや長くする。The outer inner tube 9a has an upper part formed on the inner inner tube 10a.
The diameter of the upper portion is made narrower by narrowing the upper portion of the tube in a tapered shape so as to have the same inner diameter as that of the inner inner tube 10. The inner diameter of the narrowed portion is
Equal to the inner diameter of Further, the outer inner tube 9a and the inner inner tube 1
The gap between the inner pipe 9a and the outer pipe 9a may be such that back diffusion does not occur between the outer inner pipe 9a and the inner inner pipe 10, and is, for example, 300 mm.
About 50 mm with respect to the inner diameter of the inner tube. In addition, the length of the inner inner tube 10 is set to the middle of the boat 4, and the length of the outer inner tube 9a is set to be slightly longer than the top of the boat 4.
【0014】次に、本発明の動作について、図1を用い
て説明する。本発明の縦型減圧気相成長装置では、原料
ガス、例えばSiH4とPH3を炉芯管1の下端から導
入し、排気側へと流す構造であり、炉芯管1内のガスの
流れは、ガス導入側から排気側へ向けて常に一方向とな
っている。導入された原料ガスであるSiH4およびP
H3は、ウエハ3及び内側内管10の内壁に成膜し、排
気側へガスが移動するに従いガス濃度が低下する。in
−situPドープSiの場合、P濃度の炉内均一性が
10〜20%まで低下する。Next, the operation of the present invention will be described with reference to FIG. The vertical reduced pressure vapor phase epitaxy apparatus of the present invention has a structure in which source gases, for example, SiH4 and PH3 are introduced from the lower end of the furnace core tube 1 and flow to the exhaust side. There is always one direction from the gas introduction side to the exhaust side. Introduced source gases SiH4 and P
H3 is deposited on the wafer 3 and the inner wall of the inner inner tube 10, and the gas concentration decreases as the gas moves toward the exhaust side. in
In the case of -situP-doped Si, the uniformity of the P concentration in the furnace is reduced to 10 to 20%.
【0015】そこで、本発明は、原料ガスの導入部近傍
にあるウエハ3の成膜を押さえるために、内管を二重管
にし、区切られた外側内管9aと内側内管10との間に
原料ガス、例えばPH3を流すことにより、原料ガス濃
度の低下を補う。そのために、本発明では、内側内管1
0がとぎれる部分から、外側内管9aの管径をテーパ状
に絞ることにより、この絞り部から原料ガスを合流さ
せ、炉芯管1内の排気コンダクタンスを一定に保ち、反
応炉内の反応ガスの流量及び圧力を一定に保つことが可
能となる。In order to suppress the film formation on the wafer 3 in the vicinity of the source gas introduction part, the present invention provides an inner tube having a double tube and a space between the divided outer inner tube 9a and the inner inner tube 10. The source gas, for example, PH3, is supplied to make up for a decrease in the source gas concentration. Therefore, in the present invention, the inner inner tube 1
By reducing the diameter of the outer inner tube 9a in a tapered shape from the portion where the 0 is interrupted, the raw material gas is merged from the narrowed portion, the exhaust conductance in the furnace core tube 1 is kept constant, and the reaction gas in the reactor is Can be kept constant.
【0016】この結果、本発明の実施の形態において
は、炉芯管内各位置におけるウエハの膜厚及び不純物濃
度を含めた膜質の均一性が5%まで向上した。以上、本
発明を縦型減圧気相成長装置について述べてきたが、横
型減圧気相成長装置にも適用できることはもちろんであ
る。As a result, in the embodiment of the present invention, the uniformity of the film quality including the wafer film thickness and the impurity concentration at each position in the furnace core tube has been improved to 5%. As described above, the present invention has been described with reference to the vertical type reduced pressure vapor phase epitaxy apparatus.
【0017】[0017]
【発明の効果】本発明の第1の効果は、原料ガス導入側
と排気側との、ウエハの成長膜厚及び不純物濃度などの
膜質を均一にし、製造ばらつきを低減することができる
ことである。その理由は、原料ガス導入側と排気側と
の、反応ガス濃度と反応圧力のばらつきを低減し、反応
速度を均一にすることを可能にしたからである。A first effect of the present invention is that the film quality such as the grown film thickness of the wafer and the impurity concentration can be made uniform between the source gas introduction side and the exhaust side, thereby reducing manufacturing variations. The reason is that variations in the reaction gas concentration and the reaction pressure between the source gas introduction side and the exhaust side can be reduced, and the reaction speed can be made uniform.
【0018】第2の効果は、製品の信頼性のばらつきを
低減することができることである。その理由は、第1の
効果で説明したように、膜厚、膜質を均一にすることを
可能にしたからである。A second effect is that it is possible to reduce variations in product reliability. The reason is that, as described in the first effect, it is possible to make the film thickness and film quality uniform.
【図1】本発明の実施の形態を示す縦型減圧気相成長装
置の断面図である。FIG. 1 is a cross-sectional view of a vertical reduced pressure vapor deposition apparatus showing an embodiment of the present invention.
【図2】従来の縦型減圧気相成長装置の断面図である。FIG. 2 is a cross-sectional view of a conventional vertical reduced pressure vapor deposition apparatus.
1 炉芯管 2 ヒータ 3 ウエハ 4 ボート 5 ポンプ 6 ハッチ 7 ガス導入管 8 補充ガス導入管 9、9a 外側内管 10 内側内管 DESCRIPTION OF SYMBOLS 1 Furnace tube 2 Heater 3 Wafer 4 Boat 5 Pump 6 Hatch 7 Gas introduction tube 8 Replenishment gas introduction tube 9, 9a Outer inner tube 10 Inner inner tube
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C23C 16/00 - 16/56 H01L 21/205 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) C23C 16/00-16/56 H01L 21/205
Claims (5)
填し、ボートと炉芯管との間にボートを囲む二重管構造
の内管を設置し、炉芯管内を減圧するとともに、反応ガ
スを二重管の外側内管と内側内管との間及び内側内管の
内側に導入してウエハに膜成長を行う減圧気相成長装置
において、前記二重管の外側内管を延長し、延長部をテ
ーパ状に絞り込んでその先を細くし、内管は一端側が二
重管構造であり、他端側が単管構造であることを特徴と
する減圧気相成長装置。1. A boat on which a wafer is mounted is loaded into a furnace core tube, an inner tube having a double tube structure surrounding the boat is installed between the boat and the furnace core tube, and the inside of the furnace core tube is depressurized and a reaction is performed. The gas is transferred between the outer inner pipe and the inner
In a reduced pressure vapor phase growth apparatus for growing a film on a wafer by being introduced inside , the outer inner tube of the double tube is extended, the extension is narrowed down to a tapered shape, and the tapered portion is tapered. A reduced-pressure vapor deposition apparatus having a double tube structure and a single tube structure at the other end.
内径を、内側内管の内径と等しくし、前記ウエハと内管
内径との間隔を一定としたことを特徴とする請求項1記
載の減圧気相成長装置。2. The double tube according to claim 1, wherein the inside diameter of the outer tube is made equal to the inside diameter of the inner tube, and the distance between the wafer and the inside tube is constant. 2. The reduced pressure vapor phase growth apparatus according to 1.
ガスを導入し、内側内管と外側内管との間隙には、反応
で消費されたガスを補うための補充反応ガスを導入する
ことを特徴とする請求項1記載の減圧気相成長装置。3. A main reactant gas is introduced into the inner inner tube of the double tube, and a supplementary reactant gas for supplementing gas consumed in the reaction is introduced into a gap between the inner inner tube and the outer inner tube. The reduced-pressure vapor deposition apparatus according to claim 1, wherein
を、前記テーパ部で合流させることを特徴とする請求項
3記載の減圧気相成長装置。4. The method according to claim 1, wherein the main reactant gas and the supplementary reactant gas are combined at the tapered portion.
3 pressure chemical vapor deposition apparatus as claimed.
部に対向する位置に形成したことを特徴とする請求項1
記載の減圧気相成長装置。5. The boat according to claim 1, wherein the tapered portion is formed at a position facing a substantially central portion of the boat length.
The reduced pressure vapor phase growth apparatus according to the above.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09160091A JP3076268B2 (en) | 1997-06-17 | 1997-06-17 | Low pressure vapor phase growth equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09160091A JP3076268B2 (en) | 1997-06-17 | 1997-06-17 | Low pressure vapor phase growth equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH116068A JPH116068A (en) | 1999-01-12 |
JP3076268B2 true JP3076268B2 (en) | 2000-08-14 |
Family
ID=15707672
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP09160091A Expired - Lifetime JP3076268B2 (en) | 1997-06-17 | 1997-06-17 | Low pressure vapor phase growth equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3076268B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001274107A (en) * | 2000-03-28 | 2001-10-05 | Nec Kyushu Ltd | Diffusion furnace |
US10714362B2 (en) | 2018-03-15 | 2020-07-14 | Kokusai Electric Corporation | Substrate processing apparatus and method of manufacturing semiconductor device |
US10593572B2 (en) | 2018-03-15 | 2020-03-17 | Kokusai Electric Corporation | Substrate processing apparatus and method of manufacturing semiconductor device |
-
1997
- 1997-06-17 JP JP09160091A patent/JP3076268B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH116068A (en) | 1999-01-12 |
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