JPS61275125A - Stabilizing method for hexachlorodisilane - Google Patents
Stabilizing method for hexachlorodisilaneInfo
- Publication number
- JPS61275125A JPS61275125A JP11528985A JP11528985A JPS61275125A JP S61275125 A JPS61275125 A JP S61275125A JP 11528985 A JP11528985 A JP 11528985A JP 11528985 A JP11528985 A JP 11528985A JP S61275125 A JPS61275125 A JP S61275125A
- Authority
- JP
- Japan
- Prior art keywords
- hexachlorodisilane
- purity
- silica gel
- zeolite
- distillation
- 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〕
本発明は分解しやすいヘキサクロロジシランを精製し、
安定化させる方法に関する。[Detailed Description of the Invention] [Technical Field] The present invention purifies easily decomposed hexachlorodisilane,
Concerning methods of stabilization.
近年、エレクトロニクス工業の発展に伴ない、多結晶シ
・リコンあるいはアモルファスシリコン等の半導体用シ
リコンの需要が急激に増大している。In recent years, with the development of the electronics industry, the demand for silicon for semiconductors such as polycrystalline silicon or amorphous silicon has increased rapidly.
式(1)で表わされるポリクロロシラン5inCt2n
+2(n>2) (1)は、かかる半導体装
造用原料として最近特にその重要性を増している。Polychlorosilane 5inCt2n represented by formula (1)
+2 (n>2) (1) has recently become particularly important as a raw material for semiconductor device manufacturing.
これらはそのまま熱分解してアモルファスシリコン等と
することも勿論出来るが(ベルギー特許明細書第889
523号)、更に還元して、(2)式で表わされるポリ
シランとし、
5inHzn+g (n>2) (2)
これを熱分解して半導体用シリコンを製造することが普
通である。Of course, these can be thermally decomposed as they are to produce amorphous silicon, etc. (Belgium Patent Specification No. 889)
523), further reduced to a polysilane represented by formula (2), 5inHzn+g (n>2) (2)
It is common to thermally decompose this to produce silicon for semiconductors.
しかしてポリシラン、特にジシラン(Si2Hs)は、
熱分解、グロー放電分解によりアモルファスシリコン膜
を形成する場合モノシラン(SiH4)に比較して基板
上へ形成される膜の堆積速度がはるかに大きく、かつ被
膜は電気特性に優れている等の利点があり、太陽電池用
または感光体ドラム用の原料等として今後大幅な需要増
加が期待されている(特開昭5.5−83929号)。However, polysilanes, especially disilane (Si2Hs),
When an amorphous silicon film is formed by thermal decomposition or glow discharge decomposition, there are advantages such as the deposition rate of the film formed on the substrate is much higher than that of monosilane (SiH4), and the film has excellent electrical properties. Demand is expected to increase significantly in the future as a raw material for solar cells or photoreceptor drums (Japanese Patent Laid-Open No. 5.5-83929).
ヘキサクロロジシラン自体の製造方法はよく知られてお
り、通常、カルシウムシリコン、マグネシウムシリコン
、あるいはフェロシリコン等金属とシリコンの合金の粒
子を高温で塩素化するか、またはシリコン粒子自体を高
温で塩素化することにより行なわれる(米国特許明細書
第260272時、同第2621111号、特願昭58
−65730号)。The method for producing hexachlorodisilane itself is well known and typically involves chlorinating particles of a metal-silicon alloy such as calcium silicon, magnesium silicon, or ferrosilicon at high temperatures, or by chlorinating the silicon particles themselves at high temperatures. (U.S. Pat. No. 2,602,72, U.S. Pat.
-65730).
上記反応の生成物は、n=1.2.3、・・・に対応す
る各種ポリクロロシランを含有する常温で液状の合成液
(塩素化合成液)になっている。該合成液中の各種ポリ
クロロシランの含有比率は、もちろん反応温度、送入す
る塩素ガスの濃度および滞留時間等の反応条件によって
変わり5るが、通常は、テトラクロロシラン、ヘキサク
ロロジシラン、およびオクタクロロトリシランの王者で
その組成の大部分を占めている。ヘキサクロロジシラン
は、上記塩素化合成液を常圧もしくは減圧蒸留で分離す
ることにより得ることが出来る。しかしながら蒸留精製
では、純度は高くなるが安定性のあるヘキサクロロジシ
ランを得ることは出来なかった。すなわち蒸留精製した
ヘキサクロロジシランを放置した場合、室温においても
徐々に分解が進行し四塩化珪素、塩素を始めとする分解
物が生成することを防ぐことが出来なかった。The product of the above reaction is a synthetic liquid (chlorinated synthetic liquid) that is liquid at room temperature and contains various polychlorosilanes corresponding to n=1.2.3, . The content ratio of various polychlorosilanes in the synthesis solution varies depending on the reaction conditions such as the reaction temperature, the concentration of chlorine gas introduced, and the residence time, but usually tetrachlorosilane, hexachlorodisilane, and octachlorotrisilane are used. It is the king of Silane and makes up the majority of its composition. Hexachlorodisilane can be obtained by separating the above-mentioned chlorinated synthetic solution by distillation under normal pressure or reduced pressure. However, by distillation purification, it was not possible to obtain stable hexachlorodisilane, although the purity was high. That is, when hexachlorodisilane purified by distillation is left to stand, decomposition proceeds gradually even at room temperature, and it is not possible to prevent the production of decomposed products such as silicon tetrachloride and chlorine.
ところがこのような分解物を含むヘキサクロロジシラン
を還元してジシランを合成した場合、分解物も同時に還
元される。このためジシラン中にモノシランを始めとす
る不純物が混合し、ジシランの純度が下がる、収率が下
がる等の問題があった。However, when disilane is synthesized by reducing hexachlorodisilane containing such decomposition products, the decomposition products are also reduced at the same time. For this reason, impurities such as monosilane are mixed into disilane, resulting in problems such as a decrease in the purity of disilane and a decrease in yield.
したがって、常に高純度のジシランを得るために蒸留以
外に更にヘキサクロロジシランの分解を引き起こす物質
を除去し、これを安定化する方法の開発が望まれていた
。Therefore, in order to obtain disilane of high purity at all times, it has been desired to develop a method for stabilizing hexachlorodisilane by removing substances that cause decomposition of hexachlorodisilane in addition to distillation.
今般本発明者らは、分解しやすい易分解性のヘキサクロ
ロジシランを安定化させる方法について鋭意検討した結
果、蒸留精製したヘキサクロロジシランを更にゼオライ
トもしくはシリカゲルと接触させ、精製する事により室
温で放置しておいても分解しない安定化された高純度の
ヘキサクロロジシランが得られる事を見出し本発明に到
達した。Recently, the present inventors have conducted intensive studies on a method for stabilizing hexachlorodisilane, which is easily decomposed, and found that by further contacting distilled and purified hexachlorodisilane with zeolite or silica gel and purifying it, it can be left at room temperature. The inventors have discovered that it is possible to obtain stabilized, highly pure hexachlorodisilane that does not decompose even when exposed to heat, and has thus arrived at the present invention.
本発明でいうゼオライトとは、イオン交換性を有する珪
酸塩のことで天然品でも合成品でも良い。Zeolite as used in the present invention refers to a silicate having ion exchange properties, and may be a natural product or a synthetic product.
このゼオライトを使用するに当っては前もって加熱して
吸着水分等を除去する事が好ましい。大きさについては
特に制限は無く接触に用いる装置により粉状からベレッ
ト状のものを用いる事ができる。また、シリカゲルとは
、無定型珪酸重合物のことを言い水ガラス−酸系の水溶
液から誘導されるものであればいかなる種類であっても
用いる事が出来るが、機械的強度上Xerogelタイ
プのものが好ましい。このシリカゲルを使用するに当っ
ては前もって加熱して吸着水分等を除去する事が好まし
い。またシリカゲルの大きさについても特に制限は無く
、接触に用いる装置の形態により任意の大きさのものが
用いられる。When using this zeolite, it is preferable to heat it in advance to remove adsorbed water and the like. There is no particular restriction on the size, and depending on the device used for contact, anything from powder to pellet shape can be used. Furthermore, silica gel refers to an amorphous silicic acid polymer, and any type of silica gel can be used as long as it is derived from a water glass-acid aqueous solution. is preferred. Before using this silica gel, it is preferable to heat it in advance to remove adsorbed moisture and the like. Furthermore, there is no particular restriction on the size of the silica gel, and any size can be used depending on the form of the device used for contact.
接触させる装置の形式についても特に制限は無く攪拌槽
型、固定床型、移動床型、流動床型のいずれの形式のも
のを用いることが出来る。一般的には固定床型容器にゼ
オライトもしくはシリカゲルを充填し、上方から連続し
て、処理しようとするヘキサクロロジシランを通液する
方法が好ましい。There is no particular restriction on the type of device used for contacting, and any of the following types can be used: stirred tank type, fixed bed type, moving bed type, and fluidized bed type. Generally, it is preferable to fill a fixed bed type container with zeolite or silica gel and continuously pass the hexachlorodisilane to be treated from above.
ヘキサクロロジシランをゼオライトもしくはシリカゲル
と接触させる温度については特に制限はなく5〜100
℃の範囲であれば良いが、操作性より室温付近の温度が
好ましい。また接触させる時間についても用いる装置の
形式により変わり5るが、通常1分〜50時間の範囲で
ある。There is no particular restriction on the temperature at which hexachlorodisilane is brought into contact with zeolite or silica gel;
℃ range, but a temperature around room temperature is preferred from the viewpoint of operability. The contact time also varies depending on the type of device used, but is usually in the range of 1 minute to 50 hours.
以下実施例にて本発明を説明する。The present invention will be explained below with reference to Examples.
実施例1
特願昭58−65730号、実施例1の方法により得ら
れた純度98%のヘキサクロロジシランを、更に減圧蒸
留することにより純度99.9%のヘキサクロロジシラ
ンを得た。Example 1 Hexachlorodisilane with a purity of 98% obtained by the method of Example 1 of Japanese Patent Application No. 58-65730 was further distilled under reduced pressure to obtain hexachlorodisilane with a purity of 99.9%.
次に内部を窒素で満たしたドライボックス内にて内径2
0IE111長さ20c1nで底部に焼結ガラスフィル
ターのついているガラス筒に、400℃で5時間焼成し
た径1/16インチのペレット状モレキュラーシーブ5
Aを50ゴ充填し、次に純度999%のヘキサクロロジ
シランで満たした。その後、室温にて蒸留精製したヘキ
サクロロジシランを上方より50−7時間で給液し底部
より同じ<50d/時間で抜き出した。Next, the inside diameter is 2 in a dry box filled with nitrogen.
0IE111 Pelletized molecular sieve 5 with a diameter of 1/16 inch baked at 400°C for 5 hours in a glass tube with a length of 20c1n and a sintered glass filter on the bottom.
Filled with 50 g of A, then filled with 999% pure hexachlorodisilane. Thereafter, hexachlorodisilane purified by distillation at room temperature was supplied from the top over a period of 50-7 hours, and extracted from the bottom at the same rate of <50 d/hour.
抜き出した液の純度は供給液と同じ(999%であった
。この処理液を約15℃で一箇月放置後再度分析すると
純度は999%で純度の変化は無かった。The purity of the extracted liquid was the same as that of the supplied liquid (999%). When this treated liquid was left at about 15° C. for one month and analyzed again, the purity was 999% and there was no change in purity.
比較例1
実施例1の処理に用いたヘキサクロロジシランを未処理
のまま実施例1と同様にして−・箇月放置した。−箇月
後の純度を分析したところ純度は98.7%まで低下し
ており、四塩化珪素やその他のものが生成していた。Comparative Example 1 The hexachlorodisilane used in the treatment of Example 1 was left untreated for - months in the same manner as in Example 1. When the purity was analyzed after - months, the purity had decreased to 98.7%, and silicon tetrachloride and other substances were found to have been produced.
実施例2
モレキュラーシーブ5Aの代わりに200℃で4時間焼
成処理した10〜42メツシユのシリカゲルを用いた他
は実施例1と同様に精製処理を行った。Example 2 Purification was carried out in the same manner as in Example 1, except that 10 to 42 mesh silica gel calcined at 200° C. for 4 hours was used instead of Molecular Sieve 5A.
処理直後のヘキサクロロジシラン純度は999%%実施
例1と同様にして一箇月放置後の純度は998%であり
この場合もヘキサクロロジシランは充分安定化されてい
ることがわかった。The purity of hexachlorodisilane immediately after treatment was 999%. Similarly to Example 1, the purity after standing for one month was 998%, indicating that hexachlorodisilane was sufficiently stabilized in this case as well.
Claims (2)
カゲルと接触させる事を特徴とするヘキサクロロジシラ
ンの安定化法。(1) A method for stabilizing hexachlorodisilane, which is characterized by bringing hexachlorodisilane into contact with zeolite or silica gel.
特許請求の範囲第1項記載の方法。(2) The method according to claim 1, wherein the hexachlorodisilane is purified by distillation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11528985A JPS61275125A (en) | 1985-05-30 | 1985-05-30 | Stabilizing method for hexachlorodisilane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11528985A JPS61275125A (en) | 1985-05-30 | 1985-05-30 | Stabilizing method for hexachlorodisilane |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61275125A true JPS61275125A (en) | 1986-12-05 |
Family
ID=14658973
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11528985A Pending JPS61275125A (en) | 1985-05-30 | 1985-05-30 | Stabilizing method for hexachlorodisilane |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61275125A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006109427A1 (en) * | 2005-04-07 | 2006-10-19 | Toagosei Co., Ltd. | Method for purification of disilicon hexachloride and high purity disilicon hexachloride |
WO2009047238A1 (en) * | 2007-10-09 | 2009-04-16 | Wacker Chemie Ag | Process for preparing high-purity hexachlorodisilane |
JP2022546166A (en) * | 2020-02-20 | 2022-11-04 | ワッカー ケミー アクチエンゲゼルシャフト | Process for reacting at least one partially hydrogenated chlorodisilane with a solid non-functional adsorbent to obtain hexachlorodisilane |
-
1985
- 1985-05-30 JP JP11528985A patent/JPS61275125A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006109427A1 (en) * | 2005-04-07 | 2006-10-19 | Toagosei Co., Ltd. | Method for purification of disilicon hexachloride and high purity disilicon hexachloride |
US7740822B2 (en) | 2005-04-07 | 2010-06-22 | Toagosei Co., Ltd. | Method for purification of disilicon hexachloride and high purity disilicon hexachloride |
JP5157441B2 (en) * | 2005-04-07 | 2013-03-06 | 東亞合成株式会社 | Method for purifying disilicon hexachloride |
WO2009047238A1 (en) * | 2007-10-09 | 2009-04-16 | Wacker Chemie Ag | Process for preparing high-purity hexachlorodisilane |
US8551296B2 (en) | 2007-10-09 | 2013-10-08 | Wacker Chemie Ag | Process for preparing high-purity hexachlorodisilane |
JP2022546166A (en) * | 2020-02-20 | 2022-11-04 | ワッカー ケミー アクチエンゲゼルシャフト | Process for reacting at least one partially hydrogenated chlorodisilane with a solid non-functional adsorbent to obtain hexachlorodisilane |
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