JPH0419886B2 - - Google Patents

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Publication number
JPH0419886B2
JPH0419886B2 JP58230587A JP23058783A JPH0419886B2 JP H0419886 B2 JPH0419886 B2 JP H0419886B2 JP 58230587 A JP58230587 A JP 58230587A JP 23058783 A JP23058783 A JP 23058783A JP H0419886 B2 JPH0419886 B2 JP H0419886B2
Authority
JP
Japan
Prior art keywords
gas
silane
exhaust gas
packed bed
concentration
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
Application number
JP58230587A
Other languages
Japanese (ja)
Other versions
JPS60125233A (en
Inventor
Jun Saito
Takatoshi Mitsuishi
Hiroshi Waki
Hiroji Myagawa
Hiroshige Amita
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP58230587A priority Critical patent/JPS60125233A/en
Publication of JPS60125233A publication Critical patent/JPS60125233A/en
Publication of JPH0419886B2 publication Critical patent/JPH0419886B2/ja
Granted legal-status Critical Current

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Treating Waste Gases (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はシラン系排ガスの高度処理方法に関す
る。さらに詳しくは、半導体製造用シラン系ガス
の排ガスを金属酸化物の充填層を通過させること
により、接触処理する高度排ガス処理方法に関す
る。 今日の半導体工業の発展はめざましく、超
LSI、化合物半導体、アモルフアス太陽電池な
ど、まさに日進月歩の技術革新を続けており、半
導体製造用ガス使用量も増大しつつある。 かかる半導体製造用ガス、特にモノシラン
(SiH4)、ジシラン(Si2H6)、トリシラン
(Si3H8)等のシラン系ガスは、熱分解、光分解、
プラズマ分解等の方法により、単結晶シリコン、
多結晶シリコン、アモルフアスシリコン、シリコ
ン酸化膜、シリカン窒化膜等の形成に不可欠なガ
スである。しかしながら、かかるガスは反応性、
自然発火性が強い上に、例えば、モノシランの場
合、吸収により呼吸器を激しく刺激するなど毒性
が強く、若し高濃度で外部に放出されるならば、
人体および自然環境への悪影響ははかりしれない
ものがある。そのため、我国においては、良好な
作業環境の保持、自然環境の破壊の防止を目的と
して、半導体工業における排ガス中のシラン系ガ
ス濃度の規制が強化されつつある。しかも米国に
おいては、「米国産業衛生監督官会議」がモノシ
ランの作業環境濃度を0.5ppmと設定するなど激
しい規制が実施されることになつている。 通常、半導体製造用には、水素、ヘリウム、ア
ルゴン、窒素などのガスでシラン系ガスを数%か
ら数十%に希釈したガスが用いられることが多い
が、時には、希釈しない100%のシラン系ガスが
用いられることもある。 半導体製造装置は、その膜成長の方法により常
圧法と減圧法とに大別されている。 (1) 常圧法の場合、シラン系ガスを高濃度に含む
ガスが大量に排出されるが、通常、排ガスを空
気と混合して燃焼させる様工夫された装置によ
つて処理したり、水酸化アルカリ水溶液と接触
処理する方法(特開昭56−84619号、同57−
94323号)等の手段によつてシラン系ガス濃度
をできる限り低減処理した後、大気放出してい
る。 一方、減圧法の場合は、量産性があり薄い均
一膜が得られる利点はあるが、反応室(膜形成
室)と排ガス処理装置の間に真空ポンプが介在
するため、真空ポンプに未反応シランガスが混
入してポンプの故障、劣化、発火等のトラブル
を生起する可能性がある。 このため、反応室と真空ポンプの間に高温加
熱されたアルミニウムなどの金属フイルターを
取付けシランガスを処理するなどの方法が採ら
れている(特開昭53−99071号)。 しかしながら、これら従来技術である燃焼に
よる方法、水酸化アルカリ水溶液と接触処理す
る方法あるいは金属フイルターによる処理方法
などによつて処理せる排ガス中には、尚、
5ppm以上の高濃度のシラン系ガスが残存し、
この数値は自然環境の保護、労働安全衛生上の
見地からは看過し得ないものである。 のみならず、金属フイルターを用いる方法で
は、さらに600℃以上に加熱しなければならな
いなどの制約もある。したがつて、常圧法のみ
ならず減圧法においても使用し得る方法であつ
て、かつ排ガス中のシラン系ガスを少くとも
0.5ppm、好ましくは0.1ppm程度まで完全に除
去する技術の開発が期待されているゆえんであ
る。 すなわち、本発明の目的は、半導体製造装置
の排ガス中のシラン系ガスをほぼ完全に除去す
る方法を提供することにあり、その要旨とする
ところは、かかる半導体製造装置からのシラン
系ガスを含む排ガスを、固体金属酸化物を主成
分とする充填層を通過せしめ、処理することに
よつて、排ガス中のシラン系ガスの濃度を少く
とも0.5ppm以下、好ましくは0.1ppm以下、す
なわち、実質的に含有量を零とし得る方法であ
る。 以下、本発明を詳細に説明する。 本発明の充填層に使用する固体金属酸化物とし
ては、周期律表a族の水素、フランシウムを除
く元素;a族のRaを除く元素;a族のホウ
素を除く元素;a族の炭素を除く元素;Va族
の窒素、リン、ヒ素を除く元素;b族;b
族;ランタン系およびアクチニウム系のトリウ
ム、ウランを含む遷移元素の金属元素の酸化物の
粒子が挙げられ、それらが単独で、あるいは混合
物として、または、金属を担持させたものとして
用いられる。 本発明は、前記の金属酸化物を主成分とする充
填層にシラン系ガスを含有する排ガスを通気処理
するものであるが、この場合、金属酸化物粒子を
微細なものとし0.1m2/g以上の表面積をもたせ、
シラン系ガスとの気固接触能を向上させることが
望ましい。 また、金属酸化物の排ガス処理能力を高めるた
めに充填層の加熱を行ないながら排ガスを送入す
ることが効果的である。しかしながら、該加熱は
金属酸化物の種類によつては加熱を全く必要とせ
ず、室温にても十分にその排ガス除去機能を果し
得るものもあり、また処理すべきシラン系排ガス
の濃度や目的とする除去率によつては必ずしも必
要不可欠なものではない。なお、実施例に示す如
く本発明における金属酸化物による処理法では、
充填層の温度が200℃以下で排ガス中のシラン系
ガス濃度を0.1ppm以下、すなわち、検出限界以
下に処理することができる。 本発明を実施するための充填層としては、1系
列の充填層でも十分ではあるが、充填物の再生や
交換等の操作上の観点からこれを複数並列方式と
し、それぞれを処理層、再生層とし相互に切り換
えて使用するのが望ましい。 なお、実際の半導体製造においては、シラン系
ガスによるシリコン膜にホウ素、リン等のドーピ
ングをしばしば行なうが、本発明によればかかる
ドープ用ガスとして利用されるホスフインやジボ
ラン、アルシン等のガスについてもシラン系ガス
と共に除去することができるという利点を有す
る。 以下、実施例により本発明を具体的に説明す
る。 実施例 1〜50 第1図は実施例で用いた実験装置を示す。 1は25mmφ×450mmの石英管でこれに固体金
属粒子を150ml、充填層高300mmになるように充填
し、充填層2とした。充填層の部分は電気炉3で
室温から800℃の範囲で加熱できるようになつて
いる。 純モノシランガスを窒素ガスで希釈し、所定の
濃度のモノシラン含有ガスを調整しガス溜4にた
くわえた。次いでこのガスを流量計5、ニードル
バルブ6、ポンプ7を通して固体金属酸化物(ふ
るい分けして粒径をそろえたもの)を主成分とす
る充填層2に通気処理した。充填層出口ガス8を
補集し、ガス中のモノシラン濃度を分析した。分
析は光イオン化検出器を備えたガスクロマトグラ
フにより行なつた。分離カラムはPorapak−Tで
あり、モノシランの検出限界は0.1ppmである。
実験結果を第1表に示した。なお、第1図におい
て、8はパージ用N2ガスの供給口、9は同じく
出口である。 実施例 51〜100 純ジシランガスを窒素ガスで希釈し、所定の濃
度のジシラン含有ガスを調整した。次いで、実施
例1〜50と同様の装置を使用し同様の方法で実験
を行なつた。 なお、ジシランのガスクロマトグラフによる分
析の検出限界は0.1ppmである。実験結果を第2
表に示す。 実施例 101〜110 モノシランあるいはジシランを所定濃度に窒素
ガスで希釈し、これをさらに当量の空気と混合し
部分燃焼させたガスを実施例1〜50と同様の方法
で、モノシランあるいはジシランを分析した。 実験結果を第3表に示す。 比較例 1〜12 実施例において用いたモノシランあるいはジシ
ラン含有ガスをガラス、天然水晶、銀砂の充填層
を通気し、実施例1〜50と同様の方法で実験を行
なつた。実験結果を第4表に示す。
The present invention relates to an advanced treatment method for silane-based exhaust gas. More specifically, the present invention relates to an advanced exhaust gas treatment method in which exhaust gas of a silane-based gas for semiconductor manufacturing is subjected to contact treatment by passing through a packed layer of metal oxide. The development of today's semiconductor industry is remarkable, and
Technological innovations such as LSI, compound semiconductors, and amorphous solar cells continue to advance rapidly, and the amount of gas used in semiconductor manufacturing is also increasing. Such semiconductor manufacturing gases, especially silane gases such as monosilane (SiH 4 ), disilane (Si 2 H 6 ), and trisilane (Si 3 H 8 ), can be thermally decomposed, photolyzed,
By methods such as plasma decomposition, single crystal silicon,
It is an essential gas for forming polycrystalline silicon, amorphous silicon, silicon oxide films, silica nitride films, etc. However, such gases are reactive,
In addition to being highly pyrophoric, monosilane, for example, is highly toxic as it can severely irritate the respiratory tract upon absorption, and if released to the outside in high concentrations,
The negative effects on the human body and the natural environment are immeasurable. Therefore, in Japan, regulations on the concentration of silane-based gases in exhaust gas in the semiconductor industry are being tightened for the purpose of maintaining a good working environment and preventing destruction of the natural environment. Furthermore, strict regulations are being implemented in the United States, with the American Board of Industrial Hygienists setting the concentration of monosilane in the working environment at 0.5 ppm. Normally, for semiconductor manufacturing, silane-based gases diluted from several percent to several tens of percent with gases such as hydrogen, helium, argon, and nitrogen are often used, but sometimes undiluted 100% silane-based gases are used. Gas may also be used. Semiconductor manufacturing equipment is broadly classified into normal pressure method and reduced pressure method depending on the method of film growth. (1) In the case of the normal pressure method, a large amount of gas containing a high concentration of silane gas is discharged, but it is usually treated with a device that mixes the exhaust gas with air and burns it, or oxidizes the exhaust gas. Method of contact treatment with alkaline aqueous solution (JP-A-56-84619, JP-A No. 57-
After reducing the silane gas concentration as much as possible using methods such as No. 94323), it is released into the atmosphere. On the other hand, the reduced pressure method has the advantage of being mass-producible and producing a thin, uniform film, but since a vacuum pump is interposed between the reaction chamber (film forming chamber) and the exhaust gas treatment equipment, unreacted silane gas is This can cause problems such as pump failure, deterioration, and fire. For this reason, methods have been adopted such as installing a metal filter made of aluminum or the like heated to a high temperature between the reaction chamber and the vacuum pump to treat the silane gas (Japanese Patent Laid-Open No. 53-99071). However, in the exhaust gas that can be treated by these conventional methods such as combustion, contact treatment with an aqueous alkali hydroxide solution, or treatment using a metal filter,
High concentration of silane gas of 5ppm or more remains,
This figure cannot be overlooked from the standpoint of protecting the natural environment and occupational safety and health. In addition, the method using a metal filter has additional limitations such as the need to heat it to 600°C or higher. Therefore, it is a method that can be used not only in the normal pressure method but also in the reduced pressure method, and that eliminates at least the silane gas in the exhaust gas.
This is because the development of a technology that completely removes down to 0.5 ppm, preferably 0.1 ppm is expected. That is, an object of the present invention is to provide a method for almost completely removing silane-based gas from exhaust gas from semiconductor manufacturing equipment, and the gist thereof is to provide a method for almost completely removing silane-based gas from exhaust gas from semiconductor manufacturing equipment. By passing the exhaust gas through a packed bed mainly composed of solid metal oxides and treating it, the concentration of silane gas in the exhaust gas is reduced to at least 0.5 ppm or less, preferably 0.1 ppm or less, that is, substantially This is a method that can reduce the content to zero. The present invention will be explained in detail below. The solid metal oxide used in the packed bed of the present invention includes elements other than hydrogen and francium in group a of the periodic table; elements other than Ra in group a; elements other than boron in group a; and excluding carbon in group A. Elements; Va group elements excluding nitrogen, phosphorus, and arsenic; B group; b
Group: Particles of oxides of metal elements of transition elements including lanthanum-based and actinium-based thorium and uranium, which are used alone, as a mixture, or with a metal supported thereon. In the present invention, exhaust gas containing silane gas is aerated through the packed bed mainly composed of the metal oxide, but in this case, the metal oxide particles are made fine and the particle size is 0.1 m 2 /g. With a surface area of more than
It is desirable to improve the gas-solid contact ability with silane gas. Furthermore, in order to improve the exhaust gas processing ability of the metal oxide, it is effective to feed the exhaust gas while heating the packed bed. However, depending on the type of metal oxide, there are some that do not require heating at all and can sufficiently perform their exhaust gas removal function even at room temperature. Depending on the desired removal rate, this may not necessarily be necessary. In addition, as shown in the examples, in the treatment method using a metal oxide in the present invention,
When the temperature of the packed bed is 200°C or less, the concentration of silane gas in the exhaust gas can be reduced to 0.1 ppm or less, that is, below the detection limit. Although one series of packed beds is sufficient for carrying out the present invention, from the viewpoint of operations such as regeneration and replacement of the packing material, a plurality of parallel packed beds are used, and each one is a processing layer and a regeneration layer. It is desirable to switch between them. In actual semiconductor manufacturing, a silicon film is often doped with boron, phosphorus, etc. using a silane-based gas, but according to the present invention, gases such as phosphine, diborane, arsine, etc. used as such doping gases can also be doped. It has the advantage that it can be removed together with the silane gas. Hereinafter, the present invention will be specifically explained with reference to Examples. Examples 1-50 Figure 1 shows the experimental apparatus used in the examples. 1 was a 25 mmφ x 450 mm quartz tube, and 150 ml of solid metal particles were filled in this tube so that the height of the packed bed was 300 mm to form a packed bed 2. The packed bed portion can be heated in an electric furnace 3 in a range from room temperature to 800°C. Pure monosilane gas was diluted with nitrogen gas to prepare a monosilane-containing gas at a predetermined concentration and stored in the gas reservoir 4. Next, this gas was passed through a flow meter 5, a needle valve 6, and a pump 7 to be aerated into a packed bed 2 mainly composed of solid metal oxide (sieved to have a uniform particle size). The packed bed outlet gas 8 was collected and the monosilane concentration in the gas was analyzed. Analysis was performed using a gas chromatograph equipped with a photoionization detector. The separation column is Porapak-T, and the detection limit for monosilane is 0.1 ppm.
The experimental results are shown in Table 1. In FIG. 1, 8 is a supply port for purging N 2 gas, and 9 is also an outlet. Examples 51 to 100 Pure disilane gas was diluted with nitrogen gas to adjust a disilane-containing gas at a predetermined concentration. Next, experiments were conducted in the same manner as in Examples 1 to 50 using the same apparatus. Note that the detection limit of disilane analysis by gas chromatography is 0.1 ppm. The experimental results are shown in the second
Shown in the table. Examples 101 to 110 Monosilane or disilane was diluted with nitrogen gas to a predetermined concentration, mixed with an equivalent amount of air, and partially combusted. Monosilane or disilane was analyzed in the same manner as in Examples 1 to 50. . The experimental results are shown in Table 3. Comparative Examples 1 to 12 Experiments were conducted in the same manner as Examples 1 to 50 by passing the monosilane- or disilane-containing gas used in the Examples through a packed bed of glass, natural crystal, and silver sand. The experimental results are shown in Table 4.

【表】【table】

【表】 ※不検出を示す 以下同じ
[Table] *Indicates non-detection Same below

【表】【table】

【表】【table】

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明を実施するための装置を示すフ
ローシート図である。
FIG. 1 is a flow sheet diagram showing an apparatus for carrying out the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1 半導体装置から排出されるシラン系ガスを含
む排ガスを、固体金属酸化物を主成分とする充填
層を通過せしめ、該シラン系排ガス濃度を少くと
も0.5ppm以下にまで効率よく除去することを特
徴とする排ガスの高度処理方法。
1. The exhaust gas containing the silane gas discharged from the semiconductor device is passed through a packed bed mainly composed of solid metal oxide, and the concentration of the silane exhaust gas is efficiently removed to at least 0.5 ppm or less. An advanced treatment method for exhaust gas.
JP58230587A 1983-12-08 1983-12-08 High degree treatment of exhaust gas Granted JPS60125233A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58230587A JPS60125233A (en) 1983-12-08 1983-12-08 High degree treatment of exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58230587A JPS60125233A (en) 1983-12-08 1983-12-08 High degree treatment of exhaust gas

Related Child Applications (2)

Application Number Title Priority Date Filing Date
JP5018646A Division JPH0724738B2 (en) 1993-02-05 1993-02-05 Advanced treatment agent for exhaust gas
JP5018647A Division JPH0783820B2 (en) 1993-02-05 1993-02-05 Advanced treatment method for exhaust gas

Publications (2)

Publication Number Publication Date
JPS60125233A JPS60125233A (en) 1985-07-04
JPH0419886B2 true JPH0419886B2 (en) 1992-03-31

Family

ID=16910075

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58230587A Granted JPS60125233A (en) 1983-12-08 1983-12-08 High degree treatment of exhaust gas

Country Status (1)

Country Link
JP (1) JPS60125233A (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6190726A (en) * 1984-10-12 1986-05-08 Nippon Paionikusu Kk Removing agent
JPS61129026A (en) * 1984-11-27 1986-06-17 Nippon Paionikusu Kk Purification of exhaust gas
JPS621439A (en) * 1985-06-25 1987-01-07 Nippon Paionikusu Kk Removal of noxious component
JPH0687943B2 (en) * 1986-06-03 1994-11-09 日本パイオニクス株式会社 Exhaust gas purification method
JPH0741145B2 (en) * 1986-11-28 1995-05-10 旭硝子株式会社 Etching exhaust gas removal method
JP2736662B2 (en) * 1988-11-04 1998-04-02 東芝セラミックス株式会社 Semiconductor wafer fogging prevention device
JP2539067B2 (en) * 1990-02-20 1996-10-02 富士通株式会社 Low pressure vapor phase growth equipment
JPH09239232A (en) * 1994-08-05 1997-09-16 Tadahiro Omi Method for removing hydride gas and apparatus therefor
JP2608394B2 (en) * 1995-09-21 1997-05-07 日本パイオニクス株式会社 Remover
GB9913970D0 (en) 1999-06-16 1999-08-18 Boc Group Plc Semiconductor processing exhaust abatement
JP4909614B2 (en) * 2006-03-28 2012-04-04 大陽日酸株式会社 Method and apparatus for analyzing trace impurities in hydride gas
CN112000059B (en) * 2020-08-12 2022-03-15 国能龙源环保有限公司 Automatic control system and control method for ammonia online analyzer

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3789581A (en) * 1972-04-27 1974-02-05 Gulf Research Development Co Process for initial removal of sulfur compounds from gaseous hydrocarbon feedstocks before removal of arsenic therefrom
JPS6017772B2 (en) * 1980-10-31 1985-05-07 大阪石油化学株式会社 Method for removing arsenic from hydrocarbons
JPS58122025A (en) * 1982-01-13 1983-07-20 Showa Denko Kk Treatment for waste gas of dry etching
JPS58128146A (en) * 1982-01-27 1983-07-30 Nippon Sanso Kk Absorbing agent
JPS5949822A (en) * 1982-09-14 1984-03-22 Nippon Sanso Kk Treatment of gas comtaining volatile inorganic hydride or the like

Also Published As

Publication number Publication date
JPS60125233A (en) 1985-07-04

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