JPS60247933A - Semiconductor manufacturing device - Google Patents
Semiconductor manufacturing deviceInfo
- Publication number
- JPS60247933A JPS60247933A JP10268184A JP10268184A JPS60247933A JP S60247933 A JPS60247933 A JP S60247933A JP 10268184 A JP10268184 A JP 10268184A JP 10268184 A JP10268184 A JP 10268184A JP S60247933 A JPS60247933 A JP S60247933A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- combustion chamber
- mixing chamber
- oxygen
- hole
- 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.)
- Pending
Links
Abstract
Description
【発明の詳細な説明】
(技術分野)
この発明は半導体製造装置に関し、詳しくはシリコンウ
ェハ表面に酸化シリコン膜を形成する装置において、水
素ガスを燃焼させて水蒸気を得る装置に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION (Technical Field) The present invention relates to a semiconductor manufacturing apparatus, and more particularly to an apparatus for forming a silicon oxide film on the surface of a silicon wafer, in which hydrogen gas is burned to obtain water vapor.
(従来技術)
水素・酸素ガス燃焼方法で水蒸気を得る従来の装置全第
2図に示す。この装置においては、まず、酸素流入口l
から燃焼室IKあらかじめ酸素を流すとともに、着火用
ヒータ3をオンさせて、このヒータ3が水素の着火温度
以上になるようにする。(Prior Art) A conventional apparatus for obtaining water vapor using a hydrogen/oxygen gas combustion method is shown in FIG. In this device, first, the oxygen inlet l
Oxygen is flowed in advance from the combustion chamber IK, and the ignition heater 3 is turned on so that the temperature of the heater 3 becomes higher than the ignition temperature of hydrogen.
次に、水素流入口4から水素を燃焼室2に流入させ、着
火用ヒータ3で着火、燃焼させることによシ水蒸気を発
生させ、その水蒸気を電気炉5内のプロセスチューブ6
に供給する。このプロセスチューブ6内にはシリコンウ
ェハ7が収容されてAる。このシリコンウェハ7が前記
水蒸気の供給を受けながら熱酸化処理される。Next, hydrogen is caused to flow into the combustion chamber 2 from the hydrogen inlet 4, ignited and combusted by the ignition heater 3 to generate water vapor, and the water vapor is transferred to the process tube 6 in the electric furnace 5.
supply to. A silicon wafer 7 is housed in the process tube 6. This silicon wafer 7 is thermally oxidized while being supplied with the water vapor.
ところで、上記燃焼方法において、水素対酸素の流量比
が2:1の場合においては、燃焼が緩やかに起るため、
水素炎(第2図において符号8け、その水素炎を示す)
は比較的低温(約1900℃)である。しかしながら、
燃焼室2における水素−酸素の混合比はシリコンウェハ
の酸化条件によυ異なシ、酸素過剰雰囲気での燃焼条件
が必要な場合が多く、その場合は、水素炎8は、酸素過
剰炎となQ1炎の温度は2800℃にも到達することに
なる。そして、このように炎の温iが筒温になると、水
素流入口4のノズル部の石英が軟化蒸発して、第3図(
a)に示す正常なノズル部が同図(b)に示すように変
形したり、前記蒸発した石英の不純物がシリコンウェハ
17に態形*を及はしてシリコンウェハ7の信頼性を落
とす原因となるという欠点があっに0
(発明の目的)
この発明は上記の点に纜みなされたもので、その目的は
、水素流入口のノズル部の石英の軟5L′#発を防止し
、かつ酸化条件に適した任意の雰囲気を作ることができ
る半導体製造装at−提供することにある。By the way, in the above combustion method, when the flow rate ratio of hydrogen to oxygen is 2:1, combustion occurs slowly;
Hydrogen flame (number 8 in Figure 2 indicates the hydrogen flame)
is relatively low temperature (approximately 1900°C). however,
The hydrogen-oxygen mixture ratio in the combustion chamber 2 varies depending on the oxidation conditions of the silicon wafer, and combustion conditions in an oxygen-rich atmosphere are often required. In that case, the hydrogen flame 8 becomes an oxygen-rich flame. The temperature of Q1 flame will reach 2800℃. When the flame temperature i reaches the cylinder temperature, the quartz in the nozzle part of the hydrogen inlet 4 softens and evaporates, as shown in Figure 3 (
The normal nozzle part shown in a) is deformed as shown in FIG. (Objective of the Invention) This invention is based on the above-mentioned points, and its object is to prevent soft 5L'# generation of quartz at the nozzle part of the hydrogen inlet, and An object of the present invention is to provide a semiconductor manufacturing equipment that can create any atmosphere suitable for oxidation conditions.
(発明の桁壁)
この発明の要点は、水素燃廟室と、゛過剰酸素やその他
の不燃性ガスとの混合室とを分熱したことにある。(Girder of the Invention) The key point of this invention is that the hydrogen combustion chamber and the mixing chamber for excess oxygen and other non-flammable gases are heated separately.
(実施例)
以下この発明の一実施例を図面を参照して説明する。第
1図はこの発明の一実施例を示す断i!0DKJである
。この図において、】1は燃焼室で、外壁部に着火用ヒ
ータ12が設けられ、かつ酸素流入口13と水素流入口
14が内部に開口している。(Embodiment) An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows an embodiment of the present invention. It is 0DKJ. In this figure, reference numeral 1 denotes a combustion chamber, an ignition heater 12 is provided on the outer wall, and an oxygen inlet 13 and a hydrogen inlet 14 are opened inside.
15は混合室で、分離板16によシ前記燃焼¥11と分
離して設けられる。ただし、分離板16には5smφ程
贋の穴17が形成されておシ、前記燃焼室11で発生し
た水蒸気がこの穴17を介して混合室15に供給される
ようになっている。このような混合室15には希釈用酸
素流入口18が開口する。すなわち、水素流入口14の
水素流量°と酸素流入口13の酸素流軸比を2:】とし
た時、シリコンウェハの酸化に必爽な過剰酸素、つまり
水蒸気を希釈するfc、めの酸素が希釈用酵素流入口I
8から混合m<ysのみIc流入さh7るようになって
いる。この混合室15の前記分離板16と反対側はプロ
セスナ二一’7’ ] 9に接続ざわる。このプロセス
チューブ]9の外周に電気炉20が設けられる。Reference numeral 15 denotes a mixing chamber, which is separated from the combustion chamber 11 by a separation plate 16. However, a false hole 17 of about 5 smφ is formed in the separation plate 16 so that the water vapor generated in the combustion chamber 11 is supplied to the mixing chamber 15 through this hole 17. A dilution oxygen inlet 18 opens into the mixing chamber 15 . That is, when the hydrogen flow rate of the hydrogen inlet 14 and the oxygen flow axis ratio of the oxygen inlet 13 are set to 2:], the excess oxygen necessary for oxidizing the silicon wafer, that is, the oxygen that dilutes the water vapor, is Dilution enzyme inlet I
8, only the mixture m<ys flows into Ic h7. The side of the mixing chamber 15 opposite to the separating plate 16 is connected to a process chamber 21'7'9. An electric furnace 20 is provided around the outer periphery of the process tube]9.
また、このプロセスチューブ19内にシリコンウェハ2
1が収容される。Also, a silicon wafer 2 is placed inside this process tube 19.
1 is accommodated.
このように構成さ力た装置eこおいてU」、まず酸素流
入口13および希釈用酵素流入口18より酸素を流入さ
せ、燃焼室1】と混合室15を酸素で充たすとともに、
着火用ヒータ12をオンさせて水素の発火点の600℃
以上にする。次に、水素流入口14よシ水素を流入させ
る。燃焼室11に流入した水素は、着火用ヒータ12の
熱により着火し、燃焼を開始する。水素の燃焼が確認さ
れたら着火用ヒータ12をオフする。この時、水素流入
口14からの水素流量と酸素流入口13からの飄素流人
量比を、水蒸気分子の構成比である2:1となるように
設定する。このような流量比における水素燃焼は緩やか
であり、水素炎22は約1900℃で6D、比較的低温
な炎となる。この燃焼により燃焼室11で発生した水蒸
気は、分離板16の穴17よシ混合室15に流れ、希釈
用酸素流入口】8より流入し7’(酸素と混合された上
で、プロセスチューブ19に供給される。プロセスチュ
ーブ19内にはシリコンウェハ21が収容“されておp
、このシリコンウェハ21が、前記酸素と水蒸気の混合
雰囲気中で酸化処理される。In the apparatus thus constructed, first, oxygen was introduced through the oxygen inlet 13 and the dilution enzyme inlet 18 to fill the combustion chamber 1 and the mixing chamber 15 with oxygen.
Turn on the ignition heater 12 to reach 600°C, the ignition point of hydrogen.
Do more than that. Next, hydrogen is introduced through the hydrogen inlet 14. The hydrogen that has flowed into the combustion chamber 11 is ignited by the heat of the ignition heater 12 and starts combustion. When combustion of hydrogen is confirmed, the ignition heater 12 is turned off. At this time, the ratio of the hydrogen flow rate from the hydrogen inlet 14 to the oxygen flow rate from the oxygen inlet 13 is set to 2:1, which is the composition ratio of water vapor molecules. Hydrogen combustion at such a flow rate ratio is slow, and the hydrogen flame 22 becomes a relatively low temperature flame of 6D at about 1900°C. The water vapor generated in the combustion chamber 11 by this combustion flows into the mixing chamber 15 through the hole 17 of the separation plate 16, flows into the dilution oxygen inlet 8 and 7' (after being mixed with oxygen, the water vapor flows through the process tube 19 A silicon wafer 21 is housed in the process tube 19.
This silicon wafer 21 is oxidized in the mixed atmosphere of oxygen and water vapor.
以上のようにこの発明の一実施例では、燃焼室11と混
合glsを分離したため、酸化に最適な雰囲気を供給し
つつ、燃焼室11における水素と酸素量を水蒸気分子の
構成比と同一にすることができる。したかつて、水素炎
22は酸素過剰炎の2800℃という高温にならす、緩
やかな燃焼となシ、約1900℃に抑えることができる
。このため、水素流入口14のノズル部の石英の軟質蒸
発が防止され、ノズル部が変形したシ、蒸発した石英の
不純物かシリコンウェハ21に慾影eを及ばしてシリコ
ンウェハ21の信頼性を低下させるといったことをなく
すことができる。As described above, in one embodiment of the present invention, since the combustion chamber 11 and the mixing GLS are separated, an atmosphere suitable for oxidation is supplied, and the amount of hydrogen and oxygen in the combustion chamber 11 is made the same as the composition ratio of water vapor molecules. be able to. In the past, the hydrogen flame 22 could reach a high temperature of 2,800°C, which is the temperature of an oxygen-excess flame, but it can be suppressed to about 1,900°C due to slow combustion. Therefore, soft evaporation of the quartz in the nozzle portion of the hydrogen inlet 14 is prevented, and if the nozzle portion is deformed, impurities in the evaporated quartz may affect the silicon wafer 21, reducing the reliability of the silicon wafer 21. It is possible to eliminate the problem of deterioration.
なお、上記一実施例でに、混合室15での水蒸気との混
合を希釈酸素としたが、酸化条件によっては、混合室1
5での混合ガスを、電果あるいはその他の不燃性のカス
とすることができる。In the above embodiment, diluted oxygen was mixed with water vapor in the mixing chamber 15, but depending on the oxidation conditions, the mixing chamber 1
The gas mixture in step 5 can be electrolyte or other non-flammable scum.
(発明の効果)
以上詳述したようにこの発明の装置によれば、水素燃焼
室と、該室で発生した水蒸気と不燃性カスと全混合はせ
る混合室と全分離したので、配化条件IC適した任意の
雰囲気を供給しつつ、ノズルの変形およびウェハに対す
る悪影響を防止でき、安定した酸化を行える。(Effects of the Invention) As detailed above, according to the apparatus of the present invention, the hydrogen combustion chamber is completely separated from the mixing chamber in which the water vapor and non-flammable scum generated in the chamber are completely mixed. While supplying any atmosphere suitable for IC, deformation of the nozzle and adverse effects on the wafer can be prevented, and stable oxidation can be performed.
第1図はこの発明の半轡体製造装置の一実施例を示す断
面図、第2図は従来の装置の断面図、第3図は従来の装
置における水素流入口のノズル部を取出して示す斜視図
である。
11・・・燃焼室、12・・・着火用ヒータ、13・・
・酸素流入口、14・・・水素流入口、15・・・混合
室、16・・・分離板、17・・・穴、18・・・希釈
用酸素流入口。
特許出願人 沖霜気工業株式会社
第1図
2
第2図
第3図
(0)p
(bす:ンコFig. 1 is a cross-sectional view showing an embodiment of the half body manufacturing apparatus of the present invention, Fig. 2 is a cross-sectional view of a conventional apparatus, and Fig. 3 shows a nozzle portion of the hydrogen inlet in the conventional apparatus. FIG. 11... Combustion chamber, 12... Ignition heater, 13...
- Oxygen inlet, 14... Hydrogen inlet, 15... Mixing chamber, 16... Separation plate, 17... Hole, 18... Oxygen inlet for dilution. Patent applicant: Okishimoki Kogyo Co., Ltd. Figure 1 2 Figure 2 Figure 3 (0)p
Claims (1)
得る燃焼室と、核室で発生した水蒸気と不燃性ガスとを
混合させる混合室とを分離して設けたことを特徴とする
半導体製造装置。Semiconductor manufacturing characterized by separately providing a combustion chamber that mixes and burns hydrogen gas and oxygen gas to continuously obtain water vapor, and a mixing chamber that mixes the water vapor generated in the nuclear chamber with nonflammable gas. Device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10268184A JPS60247933A (en) | 1984-05-23 | 1984-05-23 | Semiconductor manufacturing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10268184A JPS60247933A (en) | 1984-05-23 | 1984-05-23 | Semiconductor manufacturing device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60247933A true JPS60247933A (en) | 1985-12-07 |
Family
ID=14333974
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10268184A Pending JPS60247933A (en) | 1984-05-23 | 1984-05-23 | Semiconductor manufacturing device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60247933A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01319940A (en) * | 1988-06-22 | 1989-12-26 | Kimmon Mfg Co Ltd | External combustion oxidizing apparatus |
EP1160838A2 (en) * | 2000-05-31 | 2001-12-05 | Tokyo Electron Limited | Heat treatment system and method |
US7250376B2 (en) | 1997-03-05 | 2007-07-31 | Renesas Technology Corp. | Method for fabricating semiconductor integrated circuit device |
-
1984
- 1984-05-23 JP JP10268184A patent/JPS60247933A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01319940A (en) * | 1988-06-22 | 1989-12-26 | Kimmon Mfg Co Ltd | External combustion oxidizing apparatus |
US7250376B2 (en) | 1997-03-05 | 2007-07-31 | Renesas Technology Corp. | Method for fabricating semiconductor integrated circuit device |
US7799690B2 (en) | 1997-03-05 | 2010-09-21 | Renesas Electronics Corporation | Method for fabricating semiconductor integrated circuit device |
EP1160838A2 (en) * | 2000-05-31 | 2001-12-05 | Tokyo Electron Limited | Heat treatment system and method |
EP1160838A3 (en) * | 2000-05-31 | 2004-12-01 | Tokyo Electron Limited | Heat treatment system and method |
US6863732B2 (en) | 2000-05-31 | 2005-03-08 | Tokyo Electron Limited | Heat treatment system and method |
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