JPH0699128B2 - Silane refining agent and refining method - Google Patents

Silane refining agent and refining method

Info

Publication number
JPH0699128B2
JPH0699128B2 JP3063940A JP6394091A JPH0699128B2 JP H0699128 B2 JPH0699128 B2 JP H0699128B2 JP 3063940 A JP3063940 A JP 3063940A JP 6394091 A JP6394091 A JP 6394091A JP H0699128 B2 JPH0699128 B2 JP H0699128B2
Authority
JP
Japan
Prior art keywords
silane
raw material
gas
treatment agent
refining
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
JP3063940A
Other languages
Japanese (ja)
Other versions
JPH05279008A (en
Inventor
喜二 斎藤
圭之 宮本
学 佐枝
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.)
Iwatani Corp
Original Assignee
Iwatani Corp
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 Iwatani Corp filed Critical Iwatani Corp
Priority to JP3063940A priority Critical patent/JPH0699128B2/en
Publication of JPH05279008A publication Critical patent/JPH05279008A/en
Publication of JPH0699128B2 publication Critical patent/JPH0699128B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/04Hydrides of silicon
    • C01B33/046Purification

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Drying Of Gases (AREA)
  • Silicon Compounds (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、半導体の薄膜形成やア
モルファス太陽電池、感光体ドラムの製造に使用される
シランの精製処理剤及び精製方法に関し、原料シランガ
スに微量不純物として含有されるホスフィン、アルシ
ン、ジボランなどを効率良く除去できる新規なものを提
供する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a silane refining agent and a refining method used for forming a semiconductor thin film, an amorphous solar cell, and a photosensitive drum, and a phosphine contained in a raw material silane gas as a trace impurity. A novel product that can efficiently remove arsine, diborane, etc. is provided.

【0002】[0002]

【従来の技術】一般に、原料シランガスにはその製造原
料や製造工程中に水分、酸素や炭酸ガスなどが混入する
ため、従来ではゼオライトを主成分とする処理剤により
これらを除去していた。
2. Description of the Related Art Generally, raw material silane gas is mixed with water, oxygen, carbon dioxide gas and the like during the production raw material and the production process. Therefore, these have conventionally been removed by a treating agent containing zeolite as a main component.

【0003】[0003]

【発明が解決しようとする課題】ところが、上記原料シ
ランガス中には、この外にホスフィン、アルシン、ジボ
ランなどの水素化物を微量不純物として含有し、これら
はウエハー上に形成した薄膜の電気特性に悪影響を及ぼ
すなどの理由により原料ガスから除去する必要がある
が、上記ゼオライト処理剤では有効に除去できなかっ
た。
However, the raw material silane gas contains hydrides such as phosphine, arsine, and diborane as trace impurities in addition to these, which adversely affect the electrical characteristics of the thin film formed on the wafer. It is necessary to remove it from the raw material gas for some reason, but it could not be effectively removed with the above zeolite treating agent.

【0004】一方、上記ホスフィン、アルシン、ジボラ
ンなどは水酸化ナトリウム溶液等のアルカリ吸収塔やF
eCl3添着剤を充填したFeCl3吸収塔で除去するこ
とも可能であるが、アルカリ吸収塔による方式は湿式で
装置全体が大型になるうえ、除去効率も低いという問題
がある。また、FeCl3吸収塔による方式は上記アル
カリ方式より効率が高いが、原料シランガス中の不純物
含有濃度はともにサブppmオーダーの微量であって、こ
れを上述の電気特性への影響を排除できるようなppbオ
ーダー以下にまで除去することは容易ではない。本発明
は、これらの微量の不純物水素化物を精密に除去するこ
とを技術的課題とする。
On the other hand, the above-mentioned phosphine, arsine, diborane, etc. are used in an alkali absorption tower such as sodium hydroxide solution or F
It is possible to remove the FeCl 3 absorption tower filled with the eCl 3 adsorbent, but the method using the alkali absorption tower has a problem in that the entire apparatus is wet and the removal efficiency is low. Further, the method using the FeCl 3 absorption tower is more efficient than the above-mentioned alkaline method, but the impurity content concentration in the raw material silane gas is a trace amount of sub-ppm order, and it is possible to eliminate the influence on the above electrical characteristics. It is not easy to remove even below ppb order. The present invention has a technical problem of precisely removing these minute amounts of impurity hydrides.

【0005】[0005]

【課題を解決するための手段】上記課題を達成するため
の手段を以下に説明すると、本発明1は、微量不純物と
して含有されるホスフィン、アルシン、ジボランなどの
ガス状水素化物を原料シランガスから除去してシランを
精製する処理剤であって、酸化銅及び酸化亜鉛の混合物
を主成分とすることを特徴とするシランの精製処理剤で
ある。本発明2は、酸化銅及び酸化亜鉛の混合物を十分
なシランで吸着飽和させることによりシランパッシベー
ション処理した精製処理剤に原料シランガスを接触させ
て原料ガス中に微量不純物として含有されるホスフィ
ン、アルシン、ジボランなどのガス状水素化物を吸着さ
せることにより、当該微量不純物である水素化物を原料
シランガスから選択的に除去してシランを精製すること
を特徴とするシランの精製方法である。
Means for achieving the above object will be described below. In the present invention 1, gaseous hydrides such as phosphine, arsine and diborane contained as trace impurities are removed from a raw material silane gas. And a purification agent for silane, which is characterized in that it contains a mixture of copper oxide and zinc oxide as a main component. The present invention 2 is a method in which a raw material silane gas is brought into contact with a refining treatment agent subjected to silane passivation by adsorbing and saturation a mixture of copper oxide and zinc oxide with sufficient silane, and phosphine and arsine contained as trace impurities in the raw material gas A method for purifying silane, which comprises adsorbing a gaseous hydride such as diborane to selectively remove the hydride that is the trace amount of impurities from the raw material silane gas to purify silane.

【0006】[0006]

【作用】酸化銅及び酸化亜鉛の混合物は、特開昭61―
90726号公報に示すように、シラン、フッ化ケイ素
などのガス状ケイ素化合物を除去する機能があるため、
当該混合物を主成分とする精製処理剤に原料シランガス
を接触させると、精製処理剤に先ずシランが吸着飽和す
る。引き続いて原料シランガスを接触させると、精製処
理剤にはシランはもはや吸着せず、原料ガス中に含有さ
れるホスフィンなどの微量の不純物水素化物が精製処理
剤に吸着する。精製処理剤に吸着されたホスフィンなど
は、処理剤の金属酸化物の触媒作用により、水素化物か
ら酸化物に酸化固定される(例えば、AsH3→As
23)ものと推定される。この結果、原料シランガスか
ら微量の上記不純物水素化物が除去されて、シランは効
率良く精製される。
A mixture of copper oxide and zinc oxide is disclosed in JP-A-61-
As disclosed in Japanese Patent No. 90726, since it has a function of removing a gaseous silicon compound such as silane and silicon fluoride,
When the raw material silane gas is brought into contact with the purification treatment agent containing the mixture as a main component, silane is first adsorbed and saturated in the purification treatment agent. When the raw material silane gas is subsequently contacted, silane is no longer adsorbed on the purification treatment agent, and a small amount of hydride such as phosphine contained in the raw material gas is adsorbed on the purification treatment agent. The phosphine adsorbed on the purification treatment agent is oxidatively fixed from the hydride to the oxide by the catalytic action of the metal oxide of the treatment agent (for example, AsH 3 → As
2 O 3 ). As a result, a small amount of the above-mentioned impurity hydride is removed from the raw material silane gas, and the silane is efficiently purified.

【0007】[0007]

【発明の効果】上記公報にはシランなどのガス状ケイ素
化合物の除去が開示されているだけであり、酸化銅及び
酸化亜鉛の混合物を主成分とする処理剤を、微量含有不
純物であるホスフィンなどの水素化物の除去に適用して
シランを精製する技術は全く新規である。しかも、この
シランの精製処理剤は、通常の酸化物を組み合わせたも
ので安価に実施できるうえ、上記不純物水素化の含有濃
度が微量であっても良好に除去できる。また、その精製
方法にあっては、原料シランガスを当該精製処理剤に連
続的に接触させるだけなので、精製操作を簡便且つ迅速
にできる。
The above-mentioned publication only discloses the removal of gaseous silicon compounds such as silane, and the treatment agent containing a mixture of copper oxide and zinc oxide as a main component is treated with a trace amount of impurities such as phosphine. The technology for purifying silane by applying it to the removal of hydrides of is completely new. Moreover, this silane purification agent is a combination of ordinary oxides and can be implemented at low cost, and can be satisfactorily removed even if the impurity hydrogenation content is very small. Further, in the refining method, since the raw material silane gas is simply brought into contact with the refining agent, the refining operation can be simply and quickly performed.

【0008】[0008]

【実施例】銅の硝酸塩及び亜鉛の硝酸塩に炭酸ナトリウ
ム等を加えて沈殿物を生成し、これを焼成して酸化銅、
参加亜鉛混合物を得た。これを粉砕したのち、黒鉛、ゼ
ラチン等から成るバインダーと混合し、当該混合粉を打
錠成形機で球形に成形して成分比、酸化銅50wt%、酸
化亜鉛45wt%のシラン精製処理剤を調製した。この場
合、酸化銅及び酸化亜鉛は市販品を使用しても良いし、
両者をそのまま成形する替わりに、活性炭、シリカゲル
等の多孔性物質に硝酸銅水溶液及び硝酸亜鉛水溶液を夫
々含浸させて排気又は加熱し、両酸化物を多孔性物質に
担持させても差し支えない。
EXAMPLE A sodium nitrate or the like is added to copper nitrate and zinc nitrate to form a precipitate, which is then calcined to form copper oxide,
A participating zinc mixture was obtained. After crushing this, it is mixed with a binder composed of graphite, gelatin, etc., and the mixed powder is molded into a spherical shape with a tablet molding machine to prepare a silane purification treatment agent with a component ratio of 50 wt% copper oxide and 45 wt% zinc oxide. did. In this case, copper oxide and zinc oxide may be commercially available products,
Instead of molding both of them as they are, it is also possible to impregnate a porous substance such as activated carbon or silica gel with a copper nitrate aqueous solution and a zinc nitrate aqueous solution, respectively, and evacuate or heat them to support both oxides on the porous substance.

【0009】得られた精製処理剤に原料シランガスを連
続的に接触させると、先ず、原料シランガス中のシラン
が精製処理剤に吸着飽和し、もはやそれ以上の吸着がで
きない状態になる。その後、引き続いて原料シランガス
を接触させると、原料シランガス中に微量不純物として
含有されるホスフィン、アルシン、ジボランなどのガス
状水素化物が精製処理剤に吸着し、これらの不純物水素
化物を選択的に除去する。但し、実際のシラン精製装置
には、当該シラン精製処理剤を充填した反応筒の下流側
に、冒述の従来技術で示したゼオライト充填反応筒が直
列接続され、原料シランガスからさらに水分、炭酸ガ
ス、酸素などを除去するように構成される。この場合、
一つの反応筒を本精製処理剤の充填室とゼオライトの充
填室とに区画形成しても差し支えない。
When the raw material silane gas is continuously brought into contact with the obtained purification treatment agent, first, silane in the raw material silane gas is adsorbed and saturated with the purification treatment agent, and no further adsorption is possible. After that, when the raw material silane gas is subsequently contacted, gaseous hydrides such as phosphine, arsine, and diborane, which are contained as trace impurities in the raw material silane gas, are adsorbed to the purification treatment agent, and these impurity hydrides are selectively removed. To do. However, in the actual silane refining device, the zeolite-filled reaction tube shown in the above-mentioned prior art is connected in series on the downstream side of the reaction tube filled with the silane refining treatment agent, and the raw material silane gas further contains water and carbon dioxide gas. , Configured to remove oxygen, etc. in this case,
One reaction cylinder may be divided into a packing chamber for the purification treatment agent and a packing chamber for the zeolite.

【0010】そこで、本精製処理剤を使用した試験例を
述べる。通路断面積2.2cm2、通路長135cmの反応筒
に49gの上記精製処理剤を充填し、原料シランガスを
反応筒温度:室温、ガス圧760Torr、ガス空筒速度5
00hr-1の条件下で当該反応筒に流し、反応筒通過ガス
のホスフィン、アルシン、ジボランの各不純物水素化物
の濃度をガスクロマトグラフで経時的に測定した。但
し、原料として、ホスフィン3000ppm、アルシン1
700ppm、ジボラン300ppmを含むシランガスを用い
た。
Therefore, a test example using the present purification treatment agent will be described. A reaction cylinder having a passage cross-sectional area of 2.2 cm 2 and a passage length of 135 cm was charged with 49 g of the above-mentioned purification treatment agent, and the raw material silane gas was used as the reaction cylinder temperature: room temperature, gas pressure of 760 Torr, and gas empty velocity of 5
The gas was passed through the reaction tube under the condition of 00 hr- 1 and the concentration of each hydride of phosphine, arsine and diborane in the gas passing through the reaction tube was measured with a gas chromatograph over time. However, as raw materials, phosphine 3000ppm, arsine 1
Silane gas containing 700 ppm and 300 ppm of diborane was used.

【0011】この結果、原料シランガスを流し始めると
同時に、出口不純物濃度はNDとなった。尚、濃度測定
を継続したところ、上記精製処理剤は32時間経過時点
で破過を確認した。この場合、単位重量当たりの不純物
水素化物の合計除去量を概算したところ49Nl/Kgであ
った。
As a result, at the same time when the raw material silane gas was started to flow, the outlet impurity concentration became ND. When the concentration measurement was continued, breakthrough of the above-mentioned purification treatment agent was confirmed after 32 hours. In this case, the total amount of impurity hydride removed per unit weight was estimated to be 49 Nl / Kg.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 微量不純物として含有されるホスフィ
ン、アルシン、ジボランなどのガス状水素化物を原料シ
ランガスから除去してシランを精製する処理剤であっ
て、酸化銅及び酸化亜鉛の混合物を主成分とすることを
特徴とするシランの精製処理剤。
1. A treatment agent for purifying silane by removing gaseous hydrides such as phosphine, arsine, and diborane contained as trace impurities from a raw material silane gas, and containing a mixture of copper oxide and zinc oxide as a main component. A silane refining treatment agent characterized by:
【請求項2】 酸化銅及び酸化亜鉛の混合物を十分なシ
ランで吸着飽和させることによりシランパッシベーショ
ン処理した精製処理剤に原料シランガスを接触させて原
料ガス中に微量不純物として含有されるホスフィン、ア
ルシン、ジボランなどのガス状水素化物を吸着させるこ
とにより、当該微量不純物である水素化物を原料シラン
ガスから選択的に除去してシランを精製することを特徴
とするシランの精製方法。
2. A raw material silane gas is brought into contact with a purification treatment agent subjected to silane passivation by adsorbing and saturation a mixture of copper oxide and zinc oxide with sufficient silane, and phosphine and arsine contained as trace impurities in the raw material gas. A method for purifying silane, which comprises adsorbing a gaseous hydride such as diborane to selectively remove the hydride that is the trace amount of impurities from the raw material silane gas to purify silane.
JP3063940A 1991-03-04 1991-03-04 Silane refining agent and refining method Expired - Lifetime JPH0699128B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3063940A JPH0699128B2 (en) 1991-03-04 1991-03-04 Silane refining agent and refining method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3063940A JPH0699128B2 (en) 1991-03-04 1991-03-04 Silane refining agent and refining method

Publications (2)

Publication Number Publication Date
JPH05279008A JPH05279008A (en) 1993-10-26
JPH0699128B2 true JPH0699128B2 (en) 1994-12-07

Family

ID=13243850

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3063940A Expired - Lifetime JPH0699128B2 (en) 1991-03-04 1991-03-04 Silane refining agent and refining method

Country Status (1)

Country Link
JP (1) JPH0699128B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4660715B2 (en) * 2008-06-18 2011-03-30 国立大学法人大阪大学 Si purification method, Si purification apparatus, and Si purification film production apparatus

Also Published As

Publication number Publication date
JPH05279008A (en) 1993-10-26

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