JPH0670979B2 - Vapor phase growth equipment - Google Patents
Vapor phase growth equipmentInfo
- Publication number
- JPH0670979B2 JPH0670979B2 JP62239607A JP23960787A JPH0670979B2 JP H0670979 B2 JPH0670979 B2 JP H0670979B2 JP 62239607 A JP62239607 A JP 62239607A JP 23960787 A JP23960787 A JP 23960787A JP H0670979 B2 JPH0670979 B2 JP H0670979B2
- Authority
- JP
- Japan
- Prior art keywords
- phase growth
- vapor phase
- gas
- tube
- nozzle tube
- 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
- 238000001947 vapour-phase growth Methods 0.000 title claims description 30
- 239000000758 substrate Substances 0.000 claims description 40
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 6
- 229910052710 silicon Inorganic materials 0.000 claims description 6
- 239000010703 silicon Substances 0.000 claims description 6
- 239000012071 phase Substances 0.000 claims description 3
- 238000000151 deposition Methods 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 description 19
- 239000012495 reaction gas Substances 0.000 description 15
- 239000013078 crystal Substances 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000012808 vapor phase Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- 229910021417 amorphous silicon Inorganic materials 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- MROCJMGDEKINLD-UHFFFAOYSA-N dichlorosilane Chemical compound Cl[SiH2]Cl MROCJMGDEKINLD-UHFFFAOYSA-N 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229910021420 polycrystalline silicon Inorganic materials 0.000 description 1
- 229920005591 polysilicon Polymers 0.000 description 1
- 229910000077 silane Inorganic materials 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は気相成長装置に関し、特に反応容器を縦に立て
た気相成長装置に関するものである。TECHNICAL FIELD The present invention relates to a vapor phase growth apparatus, and more particularly to a vapor phase growth apparatus in which a reaction vessel is set upright.
第4図は従来の気相成長装置を示したものである。この
種の縦型の気相成長装置は種々の成膜に使われるが、以
下Siエピタキシャル成長について説明する。基板ホルダ
ー4に単結晶基板5をある間隔で水平に積み重ねる様に
保持し、減圧下で900℃〜1200℃程度に加熱してその基
板5の表面にジクロロシラン(SiN2Cl2)等のシラン系
ガス、水素(H2)及びドーピングガスを導入してエピタ
キシャル成長させるものとなっていた。FIG. 4 shows a conventional vapor phase growth apparatus. This type of vertical vapor deposition apparatus is used for various film formations, and the Si epitaxial growth will be described below. The single crystal substrates 5 are held in the substrate holder 4 so as to be stacked horizontally at a certain interval and heated to about 900 ° C. to 1200 ° C. under reduced pressure, and the surface of the substrate 5 is covered with silane such as dichlorosilane (SiN 2 Cl 2 ). A system gas, hydrogen (H 2 ) and a doping gas were introduced for epitaxial growth.
反応容器は2重構造で、外管1で真空を保持し回転する
単結晶基板5にノズル管7を用いて反応ガスを供給す
る。反応ガスは内管2の壁面に設けられた多数のガス排
出孔10を通って排出される。The reaction container has a double structure, and the nozzle tube 7 is used to supply the reaction gas to the rotating single crystal substrate 5 which holds the vacuum in the outer tube 1. The reaction gas is discharged through a number of gas discharge holes 10 provided on the wall surface of the inner pipe 2.
上述した従来の気相エピタキシャル成長装置は、基板結
晶5に反応ガスを供給するためにノズル管7に設けられ
た反応ガス放出孔10がノズル管7の円筒面上で長さ方向
に一列のみ存在しているためノズル管7から放出される
反応ガスは、反応ガス放出孔10と基板結晶5を含む水平
面内の狭い領域にしか供給されないという欠点がある。
気相成長法で基板面内の膜厚を均一にするためには、基
板表面に広い領域に、反応ガスを均一に供給する必要が
あるが、基板結晶5が大口径になり基板表面の面積が大
きくなると従来の装置では基板表面の全領域に反応ガス
を均一にすることが困難となり、基板面内の膜厚を均一
にすることができないという欠点がある。In the above-described conventional vapor phase epitaxial growth apparatus, the reaction gas discharge holes 10 provided in the nozzle tube 7 for supplying the reaction gas to the substrate crystal 5 are present on the cylindrical surface of the nozzle tube 7 in only one row in the longitudinal direction. Therefore, there is a drawback that the reaction gas discharged from the nozzle tube 7 is supplied only to a narrow region in the horizontal plane including the reaction gas discharge hole 10 and the substrate crystal 5.
In order to make the film thickness on the substrate surface uniform by the vapor phase growth method, it is necessary to uniformly supply the reaction gas to a large area on the substrate surface, but the substrate crystal 5 has a large diameter and the area of the substrate surface is large. However, in the conventional apparatus, it becomes difficult to make the reaction gas uniform over the entire area of the substrate surface, and the film thickness within the substrate surface cannot be made uniform.
本発明の気相成長装置は、内管の内部に複数枚の被気相
成長基板を所定の間隔で水平に積み重ねるように保持
し、複数のガス放出孔を有するノズル管より前記複数枚
の被気相成長基板のそれぞれの被気相成長面にほぼ平行
にガスを流し、前記内管自体の壁面に設けられた多数の
ガス排気口を介してガスを前記内管の内部から排出して
前記気相成長面に膜を気相成長させる気相成長装置であ
って、前記ノズル管の前記被気相成長基板側の側面に前
記ガス放出孔を前記ノズル管の長手方向に複数列設け、
前記複数列のガス放出孔より放出された前記ガスが前記
被気相成長面上を放射状に拡がって流れるようにしたこ
とにより前記被気相成長基板の表面に前記ガスを均一に
供給することを特徴とする。The vapor phase growth apparatus of the present invention holds a plurality of vapor phase growth substrates in an inner tube so as to be horizontally stacked at a predetermined interval, and the plurality of gas phase growth substrates are provided from a nozzle tube having a plurality of gas discharge holes. A gas is caused to flow substantially parallel to each vapor phase growth surface of the vapor phase growth substrate, and the gas is exhausted from the inside of the inner tube through a large number of gas exhaust ports provided on the wall surface of the inner tube itself. A vapor phase growth apparatus for performing vapor phase growth of a film on a vapor phase growth surface, wherein the gas discharge holes are provided in a plurality of rows in a longitudinal direction of the nozzle tube on a side surface of the nozzle tube on the side of the vapor phase growth substrate.
The gas released from the gas release holes in the plurality of rows is made to flow radially spread over the vapor phase growth surface, so that the gas is uniformly supplied to the surface of the vapor phase growth substrate. Characterize.
次に本発明について図面を参照して説明する。 Next, the present invention will be described with reference to the drawings.
第1図(a)は本発明の一実施例の気相成長装置の縦断
面図であり、第1図(b)はノズル管7を示した図であ
り、第1図(c)は第1図(b)のAA′線断面図であ
る。本装置は、装置を支えるための架台3,外管1と円筒
2から成る2重管構造の反応管、単結晶基板5を保持す
るための基板ホルダー4、抵抗加熱炉6及び反応ガスを
供給するノズル管7から構成される。反応ガスは円筒形
のノズル管7より噴出され内管壁面に設けられたガス排
気口8を通り排気口9から排気される。FIG. 1 (a) is a vertical cross-sectional view of a vapor phase growth apparatus according to an embodiment of the present invention, FIG. 1 (b) is a view showing a nozzle tube 7, and FIG. FIG. 1 is a sectional view taken along the line AA ′ of FIG. This apparatus is provided with a pedestal 3 for supporting the apparatus, a reaction tube having a double tube structure including an outer tube 1 and a cylinder 2, a substrate holder 4 for holding a single crystal substrate 5, a resistance heating furnace 6 and a reaction gas. It is composed of the nozzle tube 7. The reaction gas is ejected from a cylindrical nozzle tube 7 and is exhausted from an exhaust port 9 through a gas exhaust port 8 provided on the inner wall surface of the inner tube.
ノズル管7には第1図(b)に示すように多数の反応ガ
ス放出孔10が設けられている。この反応ガス放出孔10は
ノズル管7の基板5のある側に向いた円筒面上に複数列
(第2図では3列)設けられているため、ノズル管7か
ら噴出される反応ガスは水平面内の広い領域にわたって
ノズル管7を中心に放射状に拡大して供給される。その
ため、大口径の基板結晶5に膜成長を行なう場合であっ
ても、基板面内の膜厚を均一にすることが可能である。The nozzle tube 7 is provided with a large number of reaction gas discharge holes 10 as shown in FIG. 1 (b). Since the reaction gas discharge holes 10 are provided in a plurality of rows (3 rows in FIG. 2) on the cylindrical surface of the nozzle tube 7 facing the substrate 5, the reaction gas ejected from the nozzle tube 7 is horizontal. It is radially expanded around the nozzle tube 7 and supplied. Therefore, even when film growth is performed on the large-diameter substrate crystal 5, it is possible to make the film thickness uniform in the substrate surface.
以下に本実施例による気相成長装置を使用したエピタキ
シャル膜の成長例を説明する。基板ホルダー4に直径15
0mmのシリコン単結晶基板5を8mm間隔で100枚セット
し、1分間に5回転の回転速度(5rpm)で基板ホルダー
4を回転させ反応管内温度を抵抗加熱電気炉によって10
50℃とした。ノズル管7よりH2を20l/min、SiH2Cl2を20
0ml/min、PH3を2ml/minで流し圧力5torrでシリコン単結
晶基板5上にN型のシリコンエピタキシャル膜を5μm
成長させた。この結果を第4図に示した従来の装置でエ
ピタキシャル膜を成長させた場合の結果と比較して説明
する。第2図は従来の成長装置及び本発明の成長装置を
用いて、直径150mmφの基板5上に成長した場合の基板
面内膜厚分布を示したものである。従来の装置の場合
は、エピタキシャル膜の膜厚は、中心部60mmφの領域で
は±5%程度の膜厚分布で、外周部に向かって薄くなっ
ており周辺部を含めた面内膜厚分布は±40%であった。
これに対し、本発明の装置では、面内膜厚の均一性が著
しく改善され、面内膜厚分布±4%の良好な値が得られ
た。又、面内の抵抗分布も±3%程度の良好な結果が得
られた。An example of growing an epitaxial film using the vapor phase growth apparatus according to this example will be described below. Board holder 4 has a diameter of 15
100 pieces of 0 mm silicon single crystal substrates 5 are set at intervals of 8 mm, the substrate holder 4 is rotated at a rotation speed (5 rpm) of 5 rotations per minute, and the temperature in the reaction tube is adjusted to 10 by a resistance heating electric furnace.
It was set to 50 ° C. 20l / min to more H 2 nozzle tube 7, the SiH 2 Cl 2 20
Flowing 0 ml / min, PH 3 at 2 ml / min, pressure 5 torr and N type silicon epitaxial film 5 μm on silicon single crystal substrate 5.
I grew it. This result will be described in comparison with the result when an epitaxial film is grown by the conventional apparatus shown in FIG. FIG. 2 shows the in-plane film thickness distribution of a substrate when grown on a substrate 5 having a diameter of 150 mm using the conventional growth apparatus and the growth apparatus of the present invention. In the case of the conventional device, the thickness of the epitaxial film is about ± 5% in the central area of 60 mmφ, and the thickness decreases toward the outer periphery, and the in-plane film thickness distribution including the peripheral area is It was ± 40%.
On the other hand, in the apparatus of the present invention, the uniformity of the in-plane film thickness was remarkably improved, and a favorable value of ± 4% in the in-plane film thickness distribution was obtained. In addition, a good result was obtained in which the in-plane resistance distribution was about ± 3%.
第3図(a)〜(c)は本発明の他の実施例の説明図で
ある。前述した一実施例9においてノズル管7として円
筒管を用いたが、本発明は円筒管に限定されるものでな
いことを示すものである。第3図はノズル管7が基板側
を向いた側面が三面からなる多面体管が、各面にそれぞ
れ一列の複数のガス放出孔11を有する。このため各面か
らのガス流路線は基板面上で放射状に拡がることにな
る。FIGS. 3A to 3C are explanatory views of another embodiment of the present invention. Although the cylindrical tube is used as the nozzle tube 7 in the above-described Example 9, it is shown that the present invention is not limited to the cylindrical tube. In FIG. 3, the nozzle tube 7 is a polyhedron tube having three sides on the side facing the substrate, and each side has a plurality of gas discharge holes 11 in a row. For this reason, the gas flow path lines from the respective surfaces spread radially on the substrate surface.
本実施例によるノズル管によって一実施例と同じ条件に
よって直径150mmφの基板結晶上にシリコンエピタキシ
ャル膜を成長し基板面内の膜厚分布を±4%程度と抑え
ることができ基本的に一実施例と同じ結果を得ることが
できた。With the nozzle tube according to this embodiment, a silicon epitaxial film can be grown on a substrate crystal having a diameter of 150 mmφ under the same conditions as in the embodiment, and the film thickness distribution in the substrate surface can be suppressed to about ± 4%. I got the same result as.
以上説明したように本発明は、気相成長装置のノズル管
に設けられた複数の反応ガス放出孔が各放出孔から放出
されるガスを一本のガス流路線で示したとき基板面上で
ノズル管を中心に複数本の流路線が放射状に拡がるよう
にして、反応ガスは基板表面のほぼ全領域に均一に供給
される。その結果、基板面内の膜厚を均一にする効果が
ある。As described above, according to the present invention, when a plurality of reaction gas discharge holes provided in the nozzle tube of the vapor phase growth apparatus show the gas discharged from each discharge hole by a single gas flow path line, on the substrate surface. The reaction gas is uniformly supplied to almost the entire region of the substrate surface such that the plurality of flow path lines radially spread around the nozzle tube. As a result, there is an effect that the film thickness within the surface of the substrate is made uniform.
また、以上はシリコンエピタキシャル成長を例に説明し
てきたが、本発明の気相成長装置は各種の酸化膜、窒化
膜、ポリシリコン膜、アモルファスシリコン膜などの成
膜にも適用できるものである。さらに、加熱方式は抵抗
加熱に限らずランプ加熱、誘導加熱等の方式を用いる事
も可能であるなどその適用範囲は広く、利用価値はきわ
めて大きい。Further, although silicon epitaxial growth has been described above as an example, the vapor phase growth apparatus of the present invention can be applied to the formation of various oxide films, nitride films, polysilicon films, amorphous silicon films and the like. Furthermore, the heating method is not limited to resistance heating, and it is also possible to use lamp heating, induction heating, or the like.
第1図(a)は本発明の一実施例の気相エピタキシャル
成長装置の縦断面図、第1図(b)は本発明の一実施例
のノズル管の正面図、第1図(c)は第1図(b)のA
A′線断面図、第2図は本発明の一実施例の基板面内膜
厚分布を示す図、第3図(a)は本発明の第2の実施例
に使用するノズル管の断面図、第3図(b)は本発明の
第2の実施例に使用するノズル管の正面図、第3図
(c)は第3図(b)のAA′線断面図、第4図(a)は
従来の気相エピタキシャル成長装置の縦断面図、第4図
(b)は従来のノズル管の正面図、第4図(c)は第4
図(b)のBB′線断面図である。 1……外管、2……内管、3……架台、4……基板ホル
ダー、5……単結晶基板、6……抵抗加熱炉、7……ノ
ズル管、8……ガス排出孔、9……排気口、10……ガス
放出孔。FIG. 1 (a) is a vertical sectional view of a vapor phase epitaxial growth apparatus according to an embodiment of the present invention, FIG. 1 (b) is a front view of a nozzle tube according to an embodiment of the present invention, and FIG. A in Figure 1 (b)
A'line sectional view, FIG. 2 is a diagram showing the in-plane film thickness distribution of an embodiment of the present invention, and FIG. 3 (a) is a sectional view of a nozzle tube used in the second embodiment of the present invention. 3 (b) is a front view of a nozzle tube used in the second embodiment of the present invention, FIG. 3 (c) is a sectional view taken along the line AA 'of FIG. 3 (b), and FIG. 4 (a). ) Is a vertical sectional view of a conventional vapor phase epitaxial growth apparatus, FIG. 4 (b) is a front view of a conventional nozzle tube, and FIG. 4 (c) is a fourth view.
It is a BB 'line sectional view of a figure (b). 1 ... Outer tube, 2 ... Inner tube, 3 ... Stand, 4 ... Substrate holder, 5 ... Single crystal substrate, 6 ... Resistance heating furnace, 7 ... Nozzle tube, 8 ... Gas discharge hole, 9 ... Exhaust port, 10 ... Gas release hole.
Claims (4)
定の間隔で水平に積み重ねるように保持し、複数のガス
放出孔を有するノズル管より前記複数枚の被気相成長基
板のそれぞれの被気相成長面にほぼ平行にガスを流し、
前記内管自体の壁面に設けられた多数のガス排気口を介
してガスを前記内管の内部から排出して前記気相成長面
に膜を気相成長させる気相成長装置であって、前記ノズ
ル管の前記被気相成長基板側の側面に前記ガス放出孔を
前記ノズル管の長手方向に複数列設け、前記複数列のガ
ス放出孔より放出された前記ガスが前記被気相成長面上
を放射状に拡がって流れるようにしたことにより前記被
気相成長基板の表面に前記ガスを均一に供給することを
特徴とする気相成長装置。1. A plurality of vapor phase growth substrates are held inside an inner tube so as to be horizontally stacked at predetermined intervals, and the plurality of vapor phase growth substrates are provided from a nozzle tube having a plurality of gas discharge holes. The gas is made to flow substantially parallel to each vapor phase growth surface of
A vapor phase growth apparatus for vapor-depositing a film on the vapor phase growth surface by discharging gas from the inside of the inner tube through a large number of gas exhaust ports provided on the wall surface of the inner tube itself, The gas discharge holes are provided in a plurality of rows in the longitudinal direction of the nozzle tube on the side surface of the nozzle tube on the side of the vapor phase growth substrate, and the gas discharged from the gas discharge holes of the plurality of rows is on the gas phase growth surface. The gas phase growth apparatus is characterized in that the gas is uniformly supplied to the surface of the vapor phase growth substrate by spreading the gas radially.
囲第1項記載の気相成長装置。2. The vapor phase growth apparatus according to claim 1, wherein the nozzle tube is a cylindrical tube.
範囲第1項記載の気相成長装置。3. The vapor phase growth apparatus according to claim 1, wherein the nozzle tube is a polyhedral tube.
長である特許請求の範囲第1項記載の気相成長装置。4. The vapor phase growth apparatus according to claim 1, wherein the vapor phase growth is silicon epitaxial growth.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62239607A JPH0670979B2 (en) | 1987-09-22 | 1987-09-22 | Vapor phase growth equipment |
| DE88115622T DE3885833T2 (en) | 1987-09-22 | 1988-09-22 | Chemical vapor deposition apparatus for the production of high quality epitaxial layers with a uniform density. |
| US07/247,850 US4992301A (en) | 1987-09-22 | 1988-09-22 | Chemical vapor deposition apparatus for obtaining high quality epitaxial layer with uniform film thickness |
| EP88115622A EP0308946B1 (en) | 1987-09-22 | 1988-09-22 | Chemical vapor deposition apparatus for obtaining high quality epitaxial layer with uniform film thickness |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62239607A JPH0670979B2 (en) | 1987-09-22 | 1987-09-22 | Vapor phase growth equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6481217A JPS6481217A (en) | 1989-03-27 |
| JPH0670979B2 true JPH0670979B2 (en) | 1994-09-07 |
Family
ID=17047262
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62239607A Expired - Fee Related JPH0670979B2 (en) | 1987-09-22 | 1987-09-22 | Vapor phase growth equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0670979B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62263629A (en) * | 1986-05-12 | 1987-11-16 | Hitachi Ltd | Vapor phase growth equipment |
-
1987
- 1987-09-22 JP JP62239607A patent/JPH0670979B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6481217A (en) | 1989-03-27 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |