JPH04297030A - Chemical vapor deposition device - Google Patents
Chemical vapor deposition deviceInfo
- Publication number
- JPH04297030A JPH04297030A JP3766791A JP3766791A JPH04297030A JP H04297030 A JPH04297030 A JP H04297030A JP 3766791 A JP3766791 A JP 3766791A JP 3766791 A JP3766791 A JP 3766791A JP H04297030 A JPH04297030 A JP H04297030A
- Authority
- JP
- Japan
- Prior art keywords
- chamber
- wall
- reaction
- gas
- wafer
- 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
Links
- 238000005229 chemical vapour deposition Methods 0.000 title claims description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 claims abstract description 7
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 claims abstract description 6
- 239000012495 reaction gas Substances 0.000 claims abstract description 6
- 239000013626 chemical specie Substances 0.000 claims abstract description 5
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims 1
- 238000001947 vapour-phase growth Methods 0.000 claims 1
- 239000007795 chemical reaction product Substances 0.000 abstract description 26
- 239000007789 gas Substances 0.000 abstract description 22
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 abstract description 15
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052681 coesite Inorganic materials 0.000 abstract description 2
- 229910052906 cristobalite Inorganic materials 0.000 abstract description 2
- 239000000377 silicon dioxide Substances 0.000 abstract description 2
- 235000012239 silicon dioxide Nutrition 0.000 abstract description 2
- 229910052682 stishovite Inorganic materials 0.000 abstract description 2
- 229910052905 tridymite Inorganic materials 0.000 abstract description 2
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 10
- 230000015572 biosynthetic process Effects 0.000 description 8
- 230000007423 decrease Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- 229910000073 phosphorus hydride Inorganic materials 0.000 description 2
- -1 If it exceeds this Substances 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000001089 thermophoresis Methods 0.000 description 1
Landscapes
- Electrodes Of Semiconductors (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、化学気相成長装置に関
し、特に、半導体装置の成膜プロセスで使用する化学気
相成長装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a chemical vapor deposition apparatus, and more particularly to a chemical vapor deposition apparatus used in a film forming process for semiconductor devices.
【0002】0002
【従来の技術】図3はいわゆるポストミックスタイプの
従来の化学気相成長装置の断面側面図である。チャンバ
(1)内のウェーハステージ(2)上に設置されたウェ
ーハ(3)は、ウェーハステージ(2)内のヒータ(4
)により加熱される。そして、排気口(5)より排気を
行いつつガスヘッド(6)からはウェーハ(3)の表面
に反応ガス(B)及びO2ガス(C)が噴射される。ウ
ェーハ(3)の表面には熱化学反応により反応生成膜(
A)が形成される。2. Description of the Related Art FIG. 3 is a cross-sectional side view of a conventional chemical vapor deposition apparatus of the so-called post-mix type. The wafer (3) placed on the wafer stage (2) in the chamber (1) is heated by the heater (4) in the wafer stage (2).
) is heated by Then, while exhausting from the exhaust port (5), the reaction gas (B) and O2 gas (C) are injected from the gas head (6) onto the surface of the wafer (3). A reaction product film (
A) is formed.
【0003】0003
【発明が解決しようとする課題】ところが、この種の従
来の化学気相成長装置においては、反応ガス(B)及び
O2ガス(C)によってウェーハ(3)の表面に形成さ
れる反応生成膜(A)以外に、ウェーハステージ(2)
の周辺の成膜下限温度以上の高温部に熱化学反応によっ
て生じた反応生成膜(F)が付着する(図3参照)。ま
た、成膜下限温度以下の低温部[チャンバ(1)の天井
部やウェーハステージ(2)より離れている部分]には
、反応ガス(B)とO2ガス(C)の気相反応によって
生じた反応生成物(G)が付着する(図3参照)。これ
らの反応生成膜(F)、反応生成物(G)は付着量が多
くなると、その付着場所から剥がれ、それがウェーハ(
3)へ付着する。こうなると、製品の歩留まり低下を招
くので、定期的に装置を止めて、付着している反応生成
膜(F)、反応生成物(G)の除去を行わなければなら
ず、装置の稼働率の低下を招くという問題点があった。[Problems to be Solved by the Invention] However, in this type of conventional chemical vapor deposition apparatus, a reaction product film ( In addition to A), wafer stage (2)
A reaction product film (F) generated by a thermochemical reaction adheres to a high temperature area around the lower limit temperature for film formation (see FIG. 3). In addition, in the low temperature part below the lower limit temperature for film formation [the part away from the ceiling of the chamber (1) and the wafer stage (2)], there is a The reaction product (G) is attached (see Figure 3). When the amount of these reaction product films (F) and reaction products (G) increases, they peel off from the place where they are attached, and they are attached to the wafer (
3) Attach to. If this happens, the yield of the product will decrease, so it is necessary to periodically stop the equipment and remove the attached reaction product film (F) and reaction product (G), which reduces the operating rate of the equipment. There was a problem in that it caused a decline.
【0004】本発明は上記のような問題点を解消するた
めになされたもので、チャンバ内に不要な反応生成膜や
反応生成物が生じない化学気相成長装置を得ることを目
的とする。The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a chemical vapor deposition apparatus in which unnecessary reaction product films and reaction products are not generated in the chamber.
【0005】[0005]
【課題を解決するための手段】本発明に係る化学気相成
長装置は、反応室内で、ウェーハステージ表面に設置さ
れたウェーハを加熱しつつ、ウェーハ表面に反応ガスを
供給することにより、所望の膜を形成する化学気相成長
装置において、前記反応室の壁面を加熱する加熱手段と
、前記反応室の内壁に沿って前記ウェーハステージから
遠ざかる方向にエトキシ基またはメトキシ基を有する化
学種を噴出する噴射手段とを備えたことを特徴とする。[Means for Solving the Problems] A chemical vapor deposition apparatus according to the present invention heats a wafer placed on a wafer stage surface in a reaction chamber and supplies a reaction gas to the wafer surface. In a chemical vapor deposition apparatus for forming a film, a heating means for heating a wall surface of the reaction chamber, and a chemical species having an ethoxy group or a methoxy group are ejected along an inner wall of the reaction chamber in a direction away from the wafer stage. The invention is characterized by comprising an injection means.
【0006】[0006]
【作用】本発明においては、チャンバの壁面を加熱する
加熱手段によりチャンバの壁面を成膜下限温度以上に加
熱し、かつ反応室の内壁に沿ってウェーハステージから
遠ざかる方向にエトキシ基またはメトキシ基を有する化
学種の蒸気を噴射する噴射手段を設け、該噴射手段から
の蒸気の流量を多くすれば、不要な反応生成膜や反応生
成物の形成を防止することができる。[Operation] In the present invention, the wall surface of the chamber is heated to a temperature higher than the lower limit temperature for film formation using a heating means that heats the wall surface of the chamber, and ethoxy groups or methoxy groups are added along the inner wall of the reaction chamber in a direction away from the wafer stage. By providing an injection means for injecting vapor of the chemical species and increasing the flow rate of the vapor from the injection means, it is possible to prevent the formation of unnecessary reaction product films and reaction products.
【0007】[0007]
【実施例】図1は本発明に係る化学気相成長装置の一実
施例を示す断面側面図である。この装置はいわゆるポス
トミックスタイプのものを示している。チャンバ(1)
内のウェーハステージ(2)上に設置されたウェーハ(
3)は、ウェーハステージ(2)内のヒーター(4)に
より成膜下限温度以上に加熱される。また、ヒーター(
10)によりチャンバ(1)の壁面を近傍のガス温度以
上に加熱する。排気口(5)より排気を行いつつ、ガス
ヘッド(6)からウェーハ(3)の表面に反応ガス(B
)(例えばSiH4)及びO2ガス(C)を噴射すると
ウェーハ(3)上で反応が起こり、SiO2膜(A)と
反応生成物(G)が生じる。反応生成物(G)は周辺へ
拡散するが、この時、ウェーハステージ(2)やガスヘ
ッド(6)の周辺部のチャンバ(1)の壁面及び排気路
内壁は、前述のように加熱されているので、流れるガス
との温度差に起因する熱泳動により反応生成物(G)の
壁面への堆積は妨げられ、装置外へ排出される。DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a cross-sectional side view showing an embodiment of a chemical vapor deposition apparatus according to the present invention. This device is of the so-called post-mix type. Chamber (1)
The wafer (
3) is heated to a temperature higher than the lower limit temperature for film formation by a heater (4) in the wafer stage (2). In addition, the heater (
10) heats the wall surface of the chamber (1) to a temperature higher than the temperature of the nearby gas. While exhausting from the exhaust port (5), a reactive gas (B) is supplied from the gas head (6) to the surface of the wafer (3).
) (for example, SiH4) and O2 gas (C), a reaction occurs on the wafer (3), producing a SiO2 film (A) and a reaction product (G). The reaction product (G) diffuses to the surrounding area, but at this time, the wall surface of the chamber (1) and the inner wall of the exhaust passage around the wafer stage (2) and gas head (6) are heated as described above. Therefore, the reaction product (G) is prevented from being deposited on the wall surface due to thermophoresis caused by the temperature difference with the flowing gas, and is discharged from the apparatus.
【0008】しかし、このままだと熱化学反応により反
応生成膜(F)が生じてチャンバ(1)の内壁に付着す
ることがある。そこで、蒸気吹出口(15)からチャン
バ(1)の内壁に沿って蒸気[例えばテトラエトキシシ
ラン(TEOS)](16)を吹き出させ、チャンバ(
1)の内面及び排気路壁面付近をTEOS蒸気過剰雰囲
気にすることにより反応生成膜(F)が生じないように
することができる。However, if this continues, a reaction product film (F) may be generated due to a thermochemical reaction and adhere to the inner wall of the chamber (1). Therefore, steam [for example, tetraethoxysilane (TEOS)] (16) is blown out along the inner wall of the chamber (1) from the steam outlet (15), and the steam (16) is blown out along the inner wall of the chamber (1).
1) By creating an atmosphere with excess TEOS vapor on the inner surface and near the wall surface of the exhaust passage, it is possible to prevent the reaction product film (F) from forming.
【0009】上述のように、排気路壁面付近をTEOS
蒸気過剰雰囲気にすることで、反応生成膜(F)が生成
されないことを図2のグラフを用いて説明する。図2は
SiH4/O2流量比1/10の条件でのTEOSとS
iH4の流量の比と成膜成長速度との関係を示すグラフ
である。このグラフからわかるように、TEOS蒸気の
流量がSiH4ガスの流量の0.5倍程度となると成膜
成長速度が急激に減少を始め、そして、TEOS蒸気の
流量がSiH4ガスの流量の2倍を越えると、成膜は行
われない。これはSiH4とO2の連鎖反応を加速する
O原子をTEOSの中にあるエトキシ基がエタノールに
なることで不活性化するためである。As mentioned above, the vicinity of the exhaust passage wall is exposed to TEOS.
The fact that the reaction product film (F) is not generated by creating an atmosphere with excess steam will be explained using the graph of FIG. 2. Figure 2 shows TEOS and S under the condition of SiH4/O2 flow rate ratio 1/10.
It is a graph showing the relationship between the flow rate ratio of iH4 and the film formation growth rate. As can be seen from this graph, when the flow rate of TEOS vapor becomes about 0.5 times the flow rate of SiH4 gas, the film growth rate begins to decrease rapidly, and when the flow rate of TEOS vapor becomes about twice the flow rate of SiH4 gas, If it exceeds this, film formation will not be performed. This is because the ethoxy group in TEOS becomes ethanol and inactivates the O atom that accelerates the chain reaction between SiH4 and O2.
【0010】TEOSによる反応の不活性化の効果は、
SiH4/O2流量比が小さくなるほど大きい。従って
、反応によりSiH4が減少し、SiH4/O2流量比
の小さくなったウェーハステージ周辺部や排気路におい
て、TEOS蒸気過剰雰囲気では、反応生成膜(F)は
生成されず、反応生成膜(F)がチャンバ(1)の内壁
面に付着することがなくなる。その結果、従来のように
装置を止めてチャンバ(1)の内壁面の掃除を行う必要
がなく、装置の稼働率が低下することがなくなる。[0010] The effect of inactivation of the reaction by TEOS is as follows:
The smaller the SiH4/O2 flow rate ratio is, the larger it is. Therefore, in the TEOS vapor excess atmosphere around the wafer stage and in the exhaust passage where SiH4 is reduced due to the reaction and the SiH4/O2 flow rate ratio is small, the reaction product film (F) is not produced, and the reaction product film (F) is This prevents the particles from adhering to the inner wall surface of the chamber (1). As a result, there is no need to stop the apparatus and clean the inner wall surface of the chamber (1) as in the past, and the operating rate of the apparatus does not decrease.
【0011】なお、上記実施例においては、加熱手段と
してヒーター(10)を用いてチャンバ(1)の壁面を
加熱する場合について説明したが、他の加熱手段を用い
てもよい。また、チャンバ(1)の内壁に沿ってウェー
ハステージ(2)から遠ざかる方向に蒸気(本実施例に
おいてはTEOS蒸気)を吹き出すことができれば蒸気
吹出口(15)の位置や形状、個数は限定されない。更
に、チャンバ(1)内壁面に吹き付ける蒸気(16)と
して本実施例ではTEOS蒸気を使用したが、蒸気はN
2ガス等の不活性ガスをキャリアとして加えたものであ
ってもよい。In the above embodiment, a case has been described in which the wall surface of the chamber (1) is heated using the heater (10) as a heating means, but other heating means may be used. Further, the position, shape, and number of the steam outlet (15) are not limited as long as the steam (TEOS steam in this example) can be blown out in the direction away from the wafer stage (2) along the inner wall of the chamber (1). . Furthermore, although TEOS steam was used in this example as the steam (16) sprayed onto the inner wall surface of the chamber (1), the steam was
An inert gas such as 2 gas may be added as a carrier.
【0012】また、上記実施例では、ポストミックスタ
イプの装置について説明したが、反応ガス(B)とO2
ガス(C)をあらかじめ混合してウェーハ(3)の表面
に噴射するいわゆるプリミックスタイプのものであって
も、本発明は適用できる。[0012] In the above embodiment, a post-mix type device was explained, but the reaction gas (B) and O2
The present invention can also be applied to a so-called premix type in which the gas (C) is mixed in advance and sprayed onto the surface of the wafer (3).
【0013】更に、上記実施例では、反応ガス(B)が
SiH4ガスの場合について説明したが、PH3(ホス
フィン)やB2H6(ジボラン)を数%含むSiH4ガ
スでもよい。Further, in the above embodiment, the reaction gas (B) is SiH4 gas, but it may be SiH4 gas containing several percent of PH3 (phosphine) or B2H6 (diborane).
【0014】また、吹き出すガスとして、TEOS蒸気
を用いて説明したが、メトキシ基またはエトキシ基を有
するガスであれば、O原子不活性化効果があり、TEO
S蒸気と同様の反応抑制作用が期待できる。[0014] Furthermore, although the explanation has been made using TEOS vapor as the gas to be blown out, any gas having a methoxy group or an ethoxy group has the effect of deactivating O atoms,
It can be expected to have the same reaction suppressing effect as S vapor.
【0015】以上のように、本発明によれば、反応室の
壁面を加熱する加熱手段と、反応室の内壁に沿ってウェ
ーハステージから遠ざかる方向にエトキシ基またはメト
キシ基を有する化学種を噴射する噴射手段とを設けたの
で、反応室の壁面を成膜下限温度以上に加熱し、該蒸気
の流量を多くすれば、反応室の壁面に不要な反応生成膜
や反応生成物が付着することがない。その結果、定期的
に装置を止めてチャンバの内壁面を掃除する必要がなく
なり、装置の稼働率の向上が図れるという効果がある。As described above, according to the present invention, there is provided a heating means for heating the wall surface of the reaction chamber, and a chemical species having an ethoxy group or a methoxy group is injected along the inner wall of the reaction chamber in a direction away from the wafer stage. Since the injection means is provided, by heating the wall surface of the reaction chamber to a temperature higher than the lower limit temperature for film formation and increasing the flow rate of the vapor, unnecessary reaction product films and reaction products can be prevented from adhering to the wall surface of the reaction chamber. do not have. As a result, it is no longer necessary to periodically stop the apparatus to clean the inner wall surface of the chamber, which has the effect of improving the operating rate of the apparatus.
【図1】本発明に係る化学気相成長装置の一実施例を示
す断面側面図である。FIG. 1 is a cross-sectional side view showing an embodiment of a chemical vapor deposition apparatus according to the present invention.
【図2】図1に示した装置の動作を説明するためのグラ
フである。FIG. 2 is a graph for explaining the operation of the device shown in FIG. 1;
【図3】従来の化学気相成長装置を示す断面側面図であ
る。FIG. 3 is a cross-sectional side view showing a conventional chemical vapor deposition apparatus.
【符号の説明】 1 チャンバ 2 ウェーハステージ 4 ヒーター 6 ガスヘッド 10 ヒーター 15 蒸気吹出口 16 蒸気(TEOS) B 反応ガス C O2ガス なお、各図中同一符号は同一または相当部分を示す。[Explanation of symbols] 1 Chamber 2 Wafer stage 4 Heater 6 Gas head 10 Heater 15 Steam outlet 16 Steam (TEOS) B Reactant gas C O2 gas Note that the same reference numerals in each figure indicate the same or corresponding parts.
Claims (1)
設置されたウェーハを加熱しつつ、ウェーハ表面に反応
ガスを供給することにより、所望の膜を形成する化学気
相成長装置において、前記反応室の壁面を加熱する加熱
手段と、前記反応室の内壁に沿って前記ウェーハステー
ジから遠ざかる方向にエトキシ基またはメトキシ基を有
する化学種を噴出する噴射手段とを備えたことを特徴と
する化学気相成長装置。1. A chemical vapor deposition apparatus that forms a desired film by supplying a reaction gas to the wafer surface while heating a wafer placed on a wafer stage surface in the reaction chamber. Chemical vapor phase growth characterized by comprising a heating means for heating a wall surface and an injection means for ejecting a chemical species having an ethoxy group or a methoxy group in a direction away from the wafer stage along the inner wall of the reaction chamber. Device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3766791A JP2860174B2 (en) | 1991-03-05 | 1991-03-05 | Chemical vapor deposition equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3766791A JP2860174B2 (en) | 1991-03-05 | 1991-03-05 | Chemical vapor deposition equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04297030A true JPH04297030A (en) | 1992-10-21 |
JP2860174B2 JP2860174B2 (en) | 1999-02-24 |
Family
ID=12503986
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3766791A Expired - Fee Related JP2860174B2 (en) | 1991-03-05 | 1991-03-05 | Chemical vapor deposition equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2860174B2 (en) |
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