JPH02145767A - Method and device for cleaning vapor-growth reaction furnace - Google Patents
Method and device for cleaning vapor-growth reaction furnaceInfo
- Publication number
- JPH02145767A JPH02145767A JP29625688A JP29625688A JPH02145767A JP H02145767 A JPH02145767 A JP H02145767A JP 29625688 A JP29625688 A JP 29625688A JP 29625688 A JP29625688 A JP 29625688A JP H02145767 A JPH02145767 A JP H02145767A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- pipe
- furnace
- silicon
- reactor
- 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
- 238000004140 cleaning Methods 0.000 title claims abstract description 45
- 238000000034 method Methods 0.000 title claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 title abstract description 5
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 19
- 239000010703 silicon Substances 0.000 claims abstract description 19
- -1 silicon halide Chemical class 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 13
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 claims abstract description 12
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 6
- 239000000956 alloy Substances 0.000 claims abstract description 6
- 229910052732 germanium Inorganic materials 0.000 claims abstract description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000001257 hydrogen Substances 0.000 claims abstract description 5
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims description 21
- 239000007789 gas Substances 0.000 claims description 15
- 238000001947 vapour-phase growth Methods 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 7
- 229910000577 Silicon-germanium Inorganic materials 0.000 claims description 5
- LEVVHYCKPQWKOP-UHFFFAOYSA-N [Si].[Ge] Chemical compound [Si].[Ge] LEVVHYCKPQWKOP-UHFFFAOYSA-N 0.000 claims description 5
- 238000006722 reduction reaction Methods 0.000 claims description 3
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 abstract description 8
- 239000008246 gaseous mixture Substances 0.000 abstract description 3
- 229910008310 Si—Ge Inorganic materials 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 239000012071 phase Substances 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 3
- 150000004820 halides Chemical class 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 229910021420 polycrystalline silicon Inorganic materials 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005530 etching Methods 0.000 description 2
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- 229910000927 Ge alloy Inorganic materials 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910021417 amorphous silicon Inorganic materials 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000005502 peroxidation Methods 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 230000009528 severe injury Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、気相成長法により、モノシランとハロゲン化
ケイ素の混合気体、モノシランとハロゲン化ゲルマニウ
ムの混合気体、又はハロゲン化ケイ素から担体上にシリ
コン又は、シリコン−ゲルマニウム合金を析出させて製
造する気相成長用反応炉の内壁の洗浄方法及びその装置
に関する。Detailed Description of the Invention [Industrial Application Field] The present invention is directed to the production of a gaseous mixture of monosilane and silicon halide, a gaseous mixture of monosilane and germanium halide, or silicon halide onto a carrier by a vapor phase growth method. The present invention relates to a method and apparatus for cleaning the inner wall of a reactor for vapor phase growth in which silicon or silicon-germanium alloy is deposited and manufactured.
[従来の技術]
たとえば、多結晶シリコン製造用反応炉における洗浄に
おいては、特公昭63−27287号公報に掲げられて
いるように、弗化水素水溶液または水酸化ナトリウム水
溶液と純水を併用した洗浄方法やあるいはその装置、さ
らにこれに塩素ガスによる炉内壁のガスエツチングを組
合せたもの、あるいは水蒸気を含む空気または不活性ガ
スにより、炉内壁の付着物を加水分解し、生成した塩化
水素が結露しないうちに炉外へ放出、炉内壁の付着固形
分を不活性ガスのジェットで排出するといった洗浄方法
あるいはその装置がある。[Prior Art] For example, in cleaning a reactor for producing polycrystalline silicon, as disclosed in Japanese Patent Publication No. 63-27287, cleaning is performed using a combination of hydrogen fluoride aqueous solution or sodium hydroxide aqueous solution and pure water. A method or an apparatus thereof, and a combination thereof with gas etching of the inner wall of the furnace using chlorine gas, or a method in which deposits on the inner wall of the furnace are hydrolyzed using air containing water vapor or an inert gas, and the generated hydrogen chloride does not condense. There is a cleaning method or device that discharges the solids from the furnace or removes the solids adhering to the inside wall of the furnace using an inert gas jet.
[発明が解決しようとする課題]
しかし、このような方法あるいは装置によると、洗浄液
に用いる弗化水素や水酸化ナトリウムにより、金属製の
反応炉や洗浄用の装置が腐食され、傷みが激しく、機器
装置類の耐用期間の低下から経済的ではない。また、ガ
スエツチングを併用したり、不活性ガスジェットによる
ものにしても、付帯する装置設備が大掛かりなものにな
り、工程も複雑化して多くの時間を要していた。[Problems to be Solved by the Invention] However, according to such a method or apparatus, the metal reactor and cleaning equipment are corroded by the hydrogen fluoride and sodium hydroxide used in the cleaning liquid, causing severe damage. It is not economical because it reduces the service life of the equipment. Further, even if gas etching is used in combination or an inert gas jet is used, the accompanying equipment becomes large-scale, and the process becomes complicated and takes a lot of time.
[課題を解決するための手段]
本発明は、気相成長装置に対し、従来から用いられてい
る以上のような洗浄方法や洗浄装置のもつ問題点を解決
すべくなされたもので、モノシランとハロゲン化ケイ素
の混合気体、モノシランとハロゲン化ゲルマニウムの混
合気体、又はハロゲン化ケイ素を熱分解及び水素還元反
応により担体上にシリコン又は、シリコンゲルマニウム
合金を製造するための気相成長用反応炉の洗浄方法にお
いて、まず第一工程として、洗浄後の洗浄液のpHが4
乃至7になるよう調整し、つぎに第三工程として、2v
01%以上の過酸化水素で洗浄し、最後に第三工程とし
て、純水により洗浄することを特徴とするもので、さら
にその装置においては、多数のノズルを備えたパイプ表
面に放射上にブラシを設け、パイプの一端を回転駆動部
に連結してこのパイプを自転可能とし、さらに液体をこ
のパイプ内に送り込むための液圧送機構をパイプ端に連
結して、自転しつつ液体が前記パイプのノズルより噴射
するように構成された回転式ブラシと、噴射後の前記液
体を回収して再び前記パイプ内へと循環させる機構とを
備え、反応炉内に前記回転式ブラシを挿入して反応炉壁
を洗浄するように構成されたことを特徴とする。また、
液圧送機構には、分岐してバルブを備えた送液管を設け
、異なる組成の液体を交互に前記パイプ内へ圧送できる
よう構成するとなお効率的である。[Means for Solving the Problems] The present invention has been made to solve the problems of the above-mentioned cleaning methods and cleaning equipment that have been conventionally used for vapor phase growth equipment. Cleaning of a reactor for vapor phase growth for producing silicon or silicon-germanium alloy on a carrier by thermal decomposition and hydrogen reduction reaction of a mixed gas of silicon halide, a mixed gas of monosilane and germanium halide, or silicon halide In the method, the first step is to adjust the pH of the washing solution after washing to 4.
Adjust to 7 to 7, then as the third step, 2v
The device is characterized by cleaning with 0.1% or more hydrogen peroxide, and finally, in the third step, cleaning with pure water.Furthermore, in this equipment, a brush is applied radially onto the surface of the pipe equipped with a large number of nozzles. One end of the pipe is connected to a rotary drive unit to enable the pipe to rotate, and a liquid pressure feeding mechanism for feeding liquid into the pipe is connected to the end of the pipe, so that the liquid flows through the pipe while rotating. The rotary brush is configured to be injected from a nozzle, and a mechanism that collects the liquid after being injected and circulates it again into the pipe, and the rotary brush is inserted into the reactor. It is characterized in that it is configured to clean walls. Also,
It is more efficient if the liquid pressure feeding mechanism is provided with a liquid feeding pipe having branches and valves so that liquids of different compositions can be alternately forced into the pipe.
これを、図面によって説明すると、本発明の一実施例で
ある第1図において7で示した多数のノズルを備えたパ
イプ21の表面に放射状にブラシ1oIJ<、1けられ
、ジのパイプの一端にはモータ8、ベルト22及びロー
タリージヨイント23がら構成された回転駆動部が連結
されており、パイプ21が自転できるよう構成されてい
る。さらに、このパイプ21及びロータリージヨイント
23の上流側は分岐し、一方にはパイプ21中に液体を
送り、これを前記ノズルから噴射するためのポンプ12
及び送液管24で構成された液圧送機構が、他方には水
をパイプ21中に送り、同様に噴射するための送水管2
5が連結されている。To explain this with reference to the drawings, brushes 1oIJ<, 1 are radially cut on the surface of a pipe 21 equipped with a large number of nozzles shown at 7 in FIG. 1, which is an embodiment of the present invention. A rotary drive unit composed of a motor 8, a belt 22, and a rotary joint 23 is connected to the pipe 21 so that the pipe 21 can rotate. Furthermore, the upstream side of this pipe 21 and the rotary joint 23 are branched, and one side has a pump 12 for sending liquid into the pipe 21 and injecting it from the nozzle.
On the other hand, there is a liquid feeding mechanism composed of a liquid feeding pipe 24, which sends water into the pipe 21, and a water feeding pipe 2 for similarly injecting water.
5 are connected.
したがって、パイプ21、ノズル7及びブラシ10から
成る回転式ブラシ9は、自転しつつ液体を噴射し、表面
の放射状のブラシにより反応炉本体内壁を擦る。Therefore, the rotary brush 9 consisting of the pipe 21, the nozzle 7, and the brush 10 sprays liquid while rotating, and scrubs the inner wall of the reactor main body with the radial brush on the surface.
また、本洗浄装置には、回収タンク2oに洗浄後の過酸
化水素水をバルブ13を調節して回収し、再び前記パイ
プ内へ循環させる機構を有し、ている。Further, this cleaning device has a mechanism for recovering the hydrogen peroxide solution after cleaning into the recovery tank 2o by adjusting the valve 13 and circulating it again into the pipe.
〔作用]
モノシランの気相分解により多結晶シリコンを製造する
場合、その反応容器内壁には、いわゆるアモルファスシ
リコンが付着する。しかし、これは、吸引器のようなも
ので比較的容易に除去することができる。ところが、ハ
ロゲン化ケイ素ちいた場合、反応炉内壁には、特公昭6
3−27287号公報にも記載されているように、高沸
点の重合物が副生析出するとされており、しかも、この
重合物は吸引程度ではなかなか取り除くことができない
。[Operation] When polycrystalline silicon is produced by vapor phase decomposition of monosilane, so-called amorphous silicon adheres to the inner wall of the reaction vessel. However, this can be removed relatively easily with something like a suction device. However, when using silicon halide, the inner wall of the reactor was
As described in Japanese Patent No. 3-27287, it is said that a high boiling point polymer is precipitated as a by-product, and furthermore, this polymer is difficult to remove by suction.
本発明者は、ハロゲン化物を用いた気相分解反応により
副生ずるこうした重合物は、弱酸性から中性域で2v0
1%以上の濃度の過酸化水素により、容易に分解除去で
きることを見出し、この作用を利用することで、本発明
を完成させたものである。The present inventor has discovered that such polymers produced as by-products in gas phase decomposition reactions using halides are 2v0 in the weakly acidic to neutral range.
It was discovered that hydrogen peroxide at a concentration of 1% or more can be easily decomposed and removed, and by utilizing this effect, the present invention was completed.
[実施例1]
第1図及び第2図は、本発明の一実施例に用いられる装
置及びこれに付帯する装置を示す6モノシ、ランとハロ
ゲン化ゲルマニウムの熱分解及び水素還元反応により担
体上にシリコン−ゲルマニウム合金を成長させる工程を
終了した気相成長用反応炉本体1を、洗浄袋ra2のベ
ースフランジ3に設置した。設置後、排気ノアン4を作
動させるとともに、気相成長用反応炉本体1上部に透明
カバー5を装着した。バルブ6を開き、水をノズル7か
ら20Q1分の割合で3分間噴出し、炉内壁表面に付着
している副生成物のうち落ちやすいものを先ず回収溝に
落下させた。[Example 1] Figures 1 and 2 show an apparatus used in an example of the present invention and equipment attached thereto. The reactor main body 1 for vapor phase growth, which had undergone the step of growing a silicon-germanium alloy, was installed on the base flange 3 of the cleaning bag ra2. After installation, the exhaust nozzle 4 was operated, and a transparent cover 5 was attached to the upper part of the vapor phase growth reactor main body 1. The valve 6 was opened and water was spouted from the nozzle 7 at a rate of 20Q1 min for 3 minutes, and by-products adhering to the inner wall surface of the furnace that were easy to fall off were first allowed to fall into the collection groove.
次いで、モータ8を起動し、回転式ブラシ9を回転させ
水を供給しつつ炉内壁表面をブラシ10で擦り、10分
間水洗いした。排水のp Hが約5であることを確認し
た後、バルブ6を閉じ、バルブIIを開き、ポンプ12
を作動させて、回転式ブラシ9を回転させつつ、5%過
酸化水素水をノズル7から15Ω/分の割合で20分間
噴出して洗浄を行なった。洗浄状態を、透明カバー5か
ら目視により確認したところ、反応炉本体内壁表面に強
固に付着していた重合物が完全に分解除去されているこ
とが判ったので、ポンプ12を停止して過酸化水素水に
よる洗浄を終えた。Next, the motor 8 was started, and the rotary brush 9 was rotated to supply water while scrubbing the inner wall surface of the furnace with the brush 10 and washing with water for 10 minutes. After confirming that the pH of the wastewater is approximately 5, close valve 6, open valve II, and turn on pump 12.
was activated, and while rotating the rotary brush 9, 5% hydrogen peroxide solution was jetted from the nozzle 7 at a rate of 15 Ω/min for 20 minutes to perform cleaning. When the cleaning condition was visually checked through the transparent cover 5, it was found that the polymer that had firmly adhered to the inner wall surface of the reactor main body had been completely decomposed and removed, so the pump 12 was stopped and the peroxidation Finished cleaning with hydrogen water.
なお、過酸化水素水による洗浄中、その、排液は、バル
ブ13を回収側へ設定し、過酸化水素水の回収タンク2
0へ回収して循環利用した。In addition, during cleaning with hydrogen peroxide solution, the drained liquid is collected by setting the valve 13 to the recovery side and collecting the hydrogen peroxide solution in the recovery tank 2.
0 was recovered and recycled.
バルブ11を閉じ、バルブ13を排液側に回し、バルブ
6を開いて水で反応炉本体内を約10分間後洗いした後
、モータ8を停止させた。The valve 11 was closed, the valve 13 was turned to the drain side, the valve 6 was opened, and the inside of the reactor main body was rinsed with water for about 10 minutes, and then the motor 8 was stopped.
バルブ6を閉じ水を止め、反応炉本体lを洗浄装置2の
ベースフランジ3より取外し、第2図に示した乾燥機1
4のベースフランジ15に設置した。数箇所に空気抜き
用の孔17が間けられた透明カバー16を反応炉本体l
の上部に装着した。Close the valve 6 to stop the water, remove the reactor main body l from the base flange 3 of the cleaning device 2, and dry the dryer 1 shown in FIG.
It was installed on the base flange 15 of 4. A transparent cover 16 with air vent holes 17 in several places is attached to the reactor body l.
It was attached to the top of the.
バルブ18を閉じて、熱風発生機19を作動させ、80
℃〜100℃の熱風を、1.5+rr/分の割合で10
分間反応炉本体1の中へ流し乾燥を行なった。この間、
バルブ18を数回開け、乾燥機14のベース上に貯った
水を抜き取った。Close the valve 18, operate the hot air generator 19, and
℃~100℃ hot air at a rate of 1.5+rr/min for 10
The mixture was poured into the reactor main body 1 for a minute and dried. During this time,
The valve 18 was opened several times to drain the water that had accumulated on the base of the dryer 14.
こうして、洗浄乾燥させた反応炉本体内壁表面を観察し
たところ、付着していた重合物は完全にとり除かれた。When the inner wall surface of the reactor main body, which had been washed and dried in this way, was observed, it was found that the adhered polymer was completely removed.
またこの反応炉にてモノシランガスを熱分解し、基体に
堆積した多結晶シリコンをFZ法にて単結晶化したとこ
ろ5oooΩ・(1)の比抵抗を有した。このように、
本発明の洗浄方法及び洗浄装置が、ハロゲン化物を用い
た際の気相成長用反応炉体内壁に付着した重合物を除去
するのに極めて有効であることが確認された。Furthermore, monosilane gas was thermally decomposed in this reactor, and the polycrystalline silicon deposited on the substrate was single-crystallized by the FZ method, and it had a specific resistance of 50ooΩ·(1). in this way,
It has been confirmed that the cleaning method and cleaning apparatus of the present invention are extremely effective in removing polymers adhering to the inner wall of a reactor for vapor phase growth when a halide is used.
なお、本実施例では、モノシランとハロゲン化ゲルマニ
ウムとの混合気体の気相分解に用いた反応炉に対して、
本発明を適用したが、モノシランとハロゲン化ケイ素の
混合気体、あるいはハロゲン化ケイ素のみの気相分解に
用いた反応炉に対しても同様に適用できることを確認し
た。In this example, the reactor used for gas phase decomposition of a mixed gas of monosilane and germanium halide was
Although the present invention was applied, it was confirmed that it can be similarly applied to a reactor used for gas phase decomposition of a mixed gas of monosilane and silicon halide, or only silicon halide.
[発明の効果]
本発明によれば、従来では落しきれなかったハロゲン化
物の気相分解反応に用いた反応炉内壁の強固な重合物を
、短時間に、しかも完全に除去することができる。した
がって、気相分解によるシリコン、あるいはシリコン−
ゲルマニウム合金製造工程の所要時間が短縮され、生産
性が向上する。[Effects of the Invention] According to the present invention, it is possible to completely remove the strong polymer on the inner wall of the reactor used in the gas phase decomposition reaction of halides, which could not be completely removed in the past, in a short time. Therefore, silicon by vapor phase decomposition or silicon-
The time required for the germanium alloy manufacturing process is shortened and productivity is improved.
洗浄液として、酸やアルカリを使用しないから作業環境
も良好となる。装置類の腐食もなくなって耐用期間が伸
びるから経済性も向上する。The work environment is also good because no acid or alkali is used as the cleaning liquid. Economic efficiency is also improved because equipment corrosion is eliminated and the service life is extended.
よた、洗浄工程が単純な上、洗浄装置も大掛かりなもの
は不要であることから、容易に設置、実施できる。Furthermore, since the cleaning process is simple and no large-scale cleaning equipment is required, it can be easily installed and implemented.
第1図は、本発明の一実施例を示す気相成長用反応炉の
洗浄装置の縦断面図。
第2図は、本発明の洗浄装置に付帯する乾燥機の参考縦
断面図。
1・・・・・・・・・・・・・反応炉本体2・・・・・
・・・・・・・・洗浄装置3.15・・・・・・・・・
・ベースフランジ4・・・・・・・・・・・・・排気フ
ァン5.16・・・・・・・・・・透明カバー6.1.
1,13.18・・・・バルブ7・・・・・・・・・・
・・・ノズル
8・・・・・・・・・・・・・
9・・・・・・・・・・・・・
10・・・・・・・・・・・・・
12・・・・・・・・・・・・・
14・・・・・・・・・・・・・
17・・・・・・・・・・・・・
19・・・・・・・・・・・・・
20・・・・・・・・・・・・・
22・・・・・・・・・・・・・
23・・・・・・・・・・・・・
24・・・・・・・・・・・・・
25・・・・・・・・・・・・・FIG. 1 is a longitudinal sectional view of a cleaning device for a vapor phase growth reactor showing an embodiment of the present invention. FIG. 2 is a reference longitudinal cross-sectional view of a dryer attached to the washing device of the present invention. 1・・・・・・・・・・・・Reactor main body 2・・・・・・
・・・・・・・・・Cleaning device 3.15・・・・・・・・・
-Base flange 4...Exhaust fan 5.16...Transparent cover 6.1.
1,13.18... Valve 7...
・・・Nozzle 8・・・・・・・・・・・・・・・ 9・・・・・・・・・・・・・・・ 10・・・・・・・・・・・・ 12...・・・・・・・・・・・・ 14・・・・・・・・・・・・ 17・・・・・・・・・・・・ 19・・・・・・・・・・・・・・・ 20・・・・・・・・・・・・ 22・・・・・・・・・・・・ 23・・・・・・・・・・・・ 24・・・・・・・・・・・・・・・ 25・・・・・・・・・・・・
Claims (1)
ランとハロゲン化ゲルマニウムの混合気体、又はハロゲ
ン化ケイ素を熱分解及び水素還元反応により担体上にシ
リコン又は、シリコンゲルマニウム合金を製造するため
の気相成長用反応炉の洗浄方法において、洗浄後の洗浄
液PHが4乃至7になるまで洗浄する第一工程と、2v
ol%以上の過酸化水素で洗浄する第二工程と、純水に
より洗浄する第三工程とから成ることを特徴とする気相
成長用反応炉の洗浄方法。 2、モノシランとハロゲン化ケイ素の混合気体、モノシ
ランとハロゲン化ゲルマニウムの混合気体、又はハロゲ
ン化ケイ素を熱分解及び水素還元反応により担体上にシ
リコン又はシリコン−ゲルマニウム合金を製造するため
の気相成長用反応炉の洗浄装置において、多数のノズル
を備えたパイプ表面に放射上にブラシを設け、前記パイ
プの一端を回転駆動部に連結してこのパイプを自転可能
とし、さらに液体をこのパイプ内に送り込むための液圧
送機構をパイプ端に連結して、自転しつつ液体が前記パ
イプのノズルより噴射するように構成された回転式ブラ
シと、噴射後の前記液体を回収して再び前記パイプ内へ
と循環させる機構とを備え、反応炉内に挿入されて反応
炉壁を洗浄するよう構成されたことを特徴とする気相成
長用反応炉の洗浄装置。 3、液圧送機構には、分岐してバルブを備えた送液管を
設け、異なる組成の液体を交互に前記パイプ内へ圧送で
きるよう構成したことを特徴とする請求項2記載の気相
成長用反応炉の洗浄装置。[Claims] 1. Producing silicon or silicon germanium alloy on a carrier by thermal decomposition and hydrogen reduction reaction of a gas mixture of monosilane and silicon halide, a gas mixture of monosilane and germanium halide, or silicon halide. In the method for cleaning a reactor for vapor phase growth, a first step of cleaning until the pH of the cleaning solution after cleaning reaches 4 to 7;
1. A method for cleaning a reactor for vapor phase growth, comprising a second step of cleaning with ol% or more hydrogen peroxide, and a third step of cleaning with pure water. 2. For vapor phase growth to produce silicon or silicon-germanium alloy on a carrier by thermal decomposition and hydrogen reduction reaction of a gas mixture of monosilane and silicon halide, a gas mixture of monosilane and germanium halide, or silicon halide In a reactor cleaning device, brushes are provided radially on the surface of a pipe equipped with a large number of nozzles, one end of the pipe is connected to a rotation drive unit to enable the pipe to rotate, and liquid is further sent into the pipe. A rotary brush configured to connect a liquid pressure feeding mechanism to the end of the pipe so that the liquid is injected from the nozzle of the pipe while rotating on its own axis, and a rotary brush that collects the ejected liquid and returns it into the pipe. 1. A cleaning device for a reactor for vapor phase growth, comprising a circulating mechanism and configured to be inserted into a reactor to clean a wall of the reactor. 3. The vapor phase growth according to claim 2, characterized in that the liquid pressure feeding mechanism is provided with a liquid feeding pipe having a branched valve and is configured to be able to alternately force feed liquids of different compositions into the pipe. Reactor cleaning equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63296256A JPH0663096B2 (en) | 1988-11-25 | 1988-11-25 | Cleaning method for reactor for vapor phase growth |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63296256A JPH0663096B2 (en) | 1988-11-25 | 1988-11-25 | Cleaning method for reactor for vapor phase growth |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02145767A true JPH02145767A (en) | 1990-06-05 |
JPH0663096B2 JPH0663096B2 (en) | 1994-08-17 |
Family
ID=17831216
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63296256A Expired - Lifetime JPH0663096B2 (en) | 1988-11-25 | 1988-11-25 | Cleaning method for reactor for vapor phase growth |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0663096B2 (en) |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06272027A (en) * | 1993-03-17 | 1994-09-27 | Fuji Photo Film Co Ltd | Method for automatically cleaning vacuum deposition tank and device therefor |
JPH0758034A (en) * | 1993-08-11 | 1995-03-03 | Tokyo Electron Ltd | Gas processing apparatus and cleaning method therof |
JPH08296800A (en) * | 1994-12-30 | 1996-11-12 | L'air Liquide | Distributing method of ultra-high purity gas minimally stopping corrosion |
US7851365B1 (en) * | 2006-04-27 | 2010-12-14 | Arizona Board of Regents, a coporate body organized under Arizona Law, Acting on behalf of Arizona State Univesity | Methods for preparing semiconductor substrates and interfacial oxides thereon |
US20110232694A1 (en) * | 2008-01-25 | 2011-09-29 | Mitsubishi Materials Corporation | Reactor cleaning apparatus |
WO2012008455A1 (en) * | 2010-07-13 | 2012-01-19 | 株式会社アルバック | Film-forming apparatus and method for cleaning film-forming apparatus |
JP2014518153A (en) * | 2011-06-29 | 2014-07-28 | エムイーエムシー・エレクトロニック・マテリアルズ・ソシエタ・ペル・アチオニ | Cleaning tool for polysilicon reactor |
US9018077B2 (en) | 2009-04-30 | 2015-04-28 | Arizona Board Of Regents, A Body Corporate Of The State Of Arizona, Acting For And On Behalf Of Arizona State University | Methods for wafer bonding, and for nucleating bonding nanophases |
US9418963B2 (en) | 2012-09-25 | 2016-08-16 | Arizona Board Of Regents, A Body Corporate Of The State Of Arizona Acting For And On Behalf Of Arizona State University | Methods for wafer bonding, and for nucleating bonding nanophases |
US9589801B2 (en) | 2011-10-31 | 2017-03-07 | Arizona Board Of Regents, A Body Corporated Of The State Of Arizona, Acting For And On Behalf Of Arizona State University | Methods for wafer bonding and for nucleating bonding nanophases using wet and steam pressurization |
WO2018225497A1 (en) | 2017-06-08 | 2018-12-13 | 株式会社トクヤマ | Cleaning device and cleaning method |
WO2019003677A1 (en) * | 2017-06-30 | 2019-01-03 | 昭和電工株式会社 | Grinding apparatus and grinding method |
CN114042710A (en) * | 2021-11-10 | 2022-02-15 | 常州艾恩希纳米镀膜科技有限公司 | Be used for CVD coating reaction cavity inner wall self-cleaning brush |
CN114481095A (en) * | 2022-01-28 | 2022-05-13 | 德州智南针机械科技有限公司 | Cleaning process and equipment for internal fittings of chemical vapor deposition equipment |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58192944U (en) * | 1982-06-16 | 1983-12-22 | 株式会社東芝 | Film forming equipment for amorphous silicon photoreceptor |
-
1988
- 1988-11-25 JP JP63296256A patent/JPH0663096B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58192944U (en) * | 1982-06-16 | 1983-12-22 | 株式会社東芝 | Film forming equipment for amorphous silicon photoreceptor |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06272027A (en) * | 1993-03-17 | 1994-09-27 | Fuji Photo Film Co Ltd | Method for automatically cleaning vacuum deposition tank and device therefor |
JPH0758034A (en) * | 1993-08-11 | 1995-03-03 | Tokyo Electron Ltd | Gas processing apparatus and cleaning method therof |
KR100381822B1 (en) * | 1993-08-11 | 2003-06-27 | 동경 엘렉트론 주식회사 | A vacuum treatment apparatus and a cleaning method therefor |
JPH08296800A (en) * | 1994-12-30 | 1996-11-12 | L'air Liquide | Distributing method of ultra-high purity gas minimally stopping corrosion |
US7851365B1 (en) * | 2006-04-27 | 2010-12-14 | Arizona Board of Regents, a coporate body organized under Arizona Law, Acting on behalf of Arizona State Univesity | Methods for preparing semiconductor substrates and interfacial oxides thereon |
US9216444B2 (en) * | 2008-01-25 | 2015-12-22 | Mitsubishi Materials Corporation | Reactor cleaning apparatus |
US20110232694A1 (en) * | 2008-01-25 | 2011-09-29 | Mitsubishi Materials Corporation | Reactor cleaning apparatus |
US9018077B2 (en) | 2009-04-30 | 2015-04-28 | Arizona Board Of Regents, A Body Corporate Of The State Of Arizona, Acting For And On Behalf Of Arizona State University | Methods for wafer bonding, and for nucleating bonding nanophases |
WO2012008455A1 (en) * | 2010-07-13 | 2012-01-19 | 株式会社アルバック | Film-forming apparatus and method for cleaning film-forming apparatus |
JP5553898B2 (en) * | 2010-07-13 | 2014-07-16 | 株式会社アルバック | Film forming apparatus and method for cleaning film forming apparatus |
JP2014518153A (en) * | 2011-06-29 | 2014-07-28 | エムイーエムシー・エレクトロニック・マテリアルズ・ソシエタ・ペル・アチオニ | Cleaning tool for polysilicon reactor |
US9589801B2 (en) | 2011-10-31 | 2017-03-07 | Arizona Board Of Regents, A Body Corporated Of The State Of Arizona, Acting For And On Behalf Of Arizona State University | Methods for wafer bonding and for nucleating bonding nanophases using wet and steam pressurization |
US9418963B2 (en) | 2012-09-25 | 2016-08-16 | Arizona Board Of Regents, A Body Corporate Of The State Of Arizona Acting For And On Behalf Of Arizona State University | Methods for wafer bonding, and for nucleating bonding nanophases |
WO2018225497A1 (en) | 2017-06-08 | 2018-12-13 | 株式会社トクヤマ | Cleaning device and cleaning method |
KR20200016271A (en) | 2017-06-08 | 2020-02-14 | 가부시끼가이샤 도꾸야마 | Cleaning apparatus and cleaning method |
WO2019003677A1 (en) * | 2017-06-30 | 2019-01-03 | 昭和電工株式会社 | Grinding apparatus and grinding method |
JP2019012786A (en) * | 2017-06-30 | 2019-01-24 | 昭和電工株式会社 | Grinding device and grinding method |
CN114042710A (en) * | 2021-11-10 | 2022-02-15 | 常州艾恩希纳米镀膜科技有限公司 | Be used for CVD coating reaction cavity inner wall self-cleaning brush |
CN114481095A (en) * | 2022-01-28 | 2022-05-13 | 德州智南针机械科技有限公司 | Cleaning process and equipment for internal fittings of chemical vapor deposition equipment |
Also Published As
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---|---|
JPH0663096B2 (en) | 1994-08-17 |
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