JPH06145177A - Purification of organometallic compound - Google Patents

Purification of organometallic compound

Info

Publication number
JPH06145177A
JPH06145177A JP32359592A JP32359592A JPH06145177A JP H06145177 A JPH06145177 A JP H06145177A JP 32359592 A JP32359592 A JP 32359592A JP 32359592 A JP32359592 A JP 32359592A JP H06145177 A JPH06145177 A JP H06145177A
Authority
JP
Japan
Prior art keywords
organometallic compound
impurities
carrier gas
purification
aluminum
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
Application number
JP32359592A
Other languages
Japanese (ja)
Other versions
JP3215195B2 (en
Inventor
Koichi Tokutome
功一 徳留
Tatsuo Sakagoshi
達夫 坂越
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.)
Tosoh Finechem Corp
Original Assignee
Tosoh Finechem 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 Tosoh Finechem Corp filed Critical Tosoh Finechem Corp
Priority to JP32359592A priority Critical patent/JP3215195B2/en
Publication of JPH06145177A publication Critical patent/JPH06145177A/en
Application granted granted Critical
Publication of JP3215195B2 publication Critical patent/JP3215195B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To improve the purity of an organometallic compound useful as a raw material in the organometal gas phase growth method used in production of a compound semiconductor, etc. CONSTITUTION:This method for purifying an organometallic compound is characteristically carried out by heating the organometallic compound, removing low- boiling impurities using an inert carrier gas, analyzing the impurities in the carrier gas with time and monitoring the state of purification thereby. This method enables even an unexperienced man to efficiently remove the low-boiling impurities in the organometallic compound.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は有機金属化合物の精製方
法に関する。さらに詳細には有機金属気相成長法で化合
物半導体を製造するための有機金属化合物中の低沸点不
純物の除去方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for purifying an organometallic compound. More specifically, the present invention relates to a method for removing low boiling point impurities in an organometallic compound for producing a compound semiconductor by a metalorganic vapor phase epitaxy method.

【0002】[0002]

【従来の技術】近年、化合物半導体トランジスター等の
製造にあたり、有機金属化合物を用いた気相成長法(M
OCVD法)が採用されるようになっている。この原料
となる有機金属化合物は不純物の少ない高純度のものが
要求されている。
2. Description of the Related Art In recent years, in the production of compound semiconductor transistors and the like, a vapor phase growth method (M
The OCVD method) has been adopted. The organometallic compound as the raw material is required to have a high purity with few impurities.

【0003】従来の精製法としてはズールナル・プリク
ラドノイ・キミイ(ZhurnalPrikladnoi Khimii),48(8),
1810(1975) に記載されているようなトリメチルガリウ
ムを精密蒸留する方法や、ジャーナル・オブ・クリスタ
ル・グロース(Journal of Crystal Growth),77,19(19
86) に記載されているようなトリメチルインジウムとダ
イフォスフィンを反応させて付加体とし蒸気圧の高い低
沸点不純物を蒸留で除く方法などがある。
As a conventional refining method, Zhurnal Prikladnoi Khimii, 48 (8),
1810 (1975) for precision distillation of trimethylgallium and Journal of Crystal Growth, 77, 19 (19
As described in 86), there is a method in which trimethylindium and diphosphine are reacted to form an adduct, and low boiling point impurities having a high vapor pressure are removed by distillation.

【0004】[0004]

【発明が解決しようとする課題】このように従来の精製
法は蒸留が基本となっているが、蒸留塔の塔頂温度では
ごく微量の不純物の分離は制御できない。このため初留
を抜き出す条件などは経験的なものになっていた。
As described above, the conventional purification method is based on distillation, but the separation of a very small amount of impurities cannot be controlled at the top temperature of the distillation column. For this reason, the conditions for extracting Hatsudome were empirical.

【0005】[0005]

【課題を解決するための手段】本発明は以上のことに鑑
み種々検討した結果、より効率的に有機金属化合物を精
製する方法を開発したもので、有機金属化合物中の低沸
点不純物を不活性なキャリアーガスを用いて除去し、こ
のキャリアーガス中の不純物を経時的に測定することで
精製状況をモニターすることを特徴とするものである。
As a result of various investigations in view of the above, the present invention has developed a method for purifying an organometallic compound more efficiently, and is capable of inactivating low boiling impurities in an organometallic compound. It is characterized in that the purification condition is monitored by removing the impurities in the carrier gas and measuring impurities in the carrier gas with time.

【0006】以下本発明を更に詳しく説明する。本発明
の有機金属化合物はそのままでも、またはその他の反応
剤を加えて付加体などにしても良い。また処理温度は特
に限定されるものではないが低沸点の不純物のみを除去
するので、好ましくは精製される有機金属化合物あるい
はその付加体の沸点より低い温度で加熱することが望ま
しい。そして加熱により気化した低沸点の不純物は不活
性なキャリアーガスによって系外に除去される。
The present invention will be described in more detail below. The organometallic compound of the present invention may be used as it is, or may be added to another reactant to form an adduct. The treatment temperature is not particularly limited, but it is desirable to heat at a temperature lower than the boiling point of the organometallic compound or its adduct to be purified, since only low boiling point impurities are removed. Then, the low boiling point impurities vaporized by heating are removed to the outside of the system by an inert carrier gas.

【0007】このような本発明の精製法を実施する装置
の一例を図1に示す。即ち4口フラスコ(2)等の容器
内に精製しようとする有機金属化合物を収納し、該フラ
スコ(2)をマントルヒーター等(4)で加熱し、且つ
フラスコ(2)内を攪拌機(3)で攪拌しながら、流量
計(1)で流量調整された窒素ガス等のキャリアーガス
をフラスコ(2)内に導入する。
An example of an apparatus for carrying out such a purification method of the present invention is shown in FIG. That is, the organometallic compound to be purified is placed in a container such as a four-necked flask (2), the flask (2) is heated by a mantle heater or the like (4), and the inside of the flask (2) is stirred by a stirrer (3). A carrier gas such as nitrogen gas having a flow rate adjusted by the flow meter (1) is introduced into the flask (2) while being stirred.

【0008】他方フラスコ(2)からのキャリアーガス
の出口配管はテープヒーター(7)で加温しておき、途
中に硝酸トラップ(5)を設けてキャリアーガス中の低
沸点有機金属不純物を捕集する。さらに上記トラップ
(5)を通過したキャリアーガスはガスクロマトグラム
のFID検出器(6)に導入し、該検出器(6)で有機
不純物を検出することにより精製状況をモニターする。
On the other hand, the outlet pipe of the carrier gas from the flask (2) is heated by a tape heater (7) and a nitric acid trap (5) is provided on the way to collect low boiling point organometallic impurities in the carrier gas. To do. Further, the carrier gas that has passed through the trap (5) is introduced into the FID detector (6) of the gas chromatogram, and the purification status is monitored by detecting organic impurities with the detector (6).

【0009】本発明の特徴はキャリアーガスを用いるこ
とで非平衡状態を常に作り出すことができ、気化した低
沸点不純物を連続して除去できることにある。さらに、
除去された不純物を測定するのにキャリアーガスをその
まま測定装置、たとえば誘導プラズマ発光分析装置(I
CP)や原子吸光分析装置などに導入したり、一旦、酸
やコールドトラップなどに捕集してから種々の分析装置
で測定するためのサンプル調製をしたりすることができ
る。不純物の除去はキャリアーガスを止めることで任意
の時点で中断することができキャリアーガスを流せばす
ぐに再開される。
A feature of the present invention is that a nonequilibrium state can be always created by using a carrier gas, and vaporized low boiling point impurities can be continuously removed. further,
To measure the removed impurities, the carrier gas is used as it is as a measuring device, for example, an induction plasma emission spectrometer (I
CP) or an atomic absorption spectrophotometer, or the like, or once collected in an acid or a cold trap and then prepared as a sample for measurement by various analyzers. The removal of impurities can be interrupted at any time by stopping the carrier gas, and restarted immediately after flowing the carrier gas.

【0010】このようにして低沸点不純物が無くなった
ことを確認してから、通常の蒸留操作を行なえば確実に
精製できる。
After confirming that the low-boiling-point impurities have been eliminated in this way, a normal distillation operation can be carried out to ensure the purification.

【0011】本発明の対象となるアルミニウム、ガリウ
ム及びインジウムの有機金属化合物は一般式Ra MX
3-a (式中、Rは炭素数が1〜4のアルキル基、Mはア
ルミニウム、ガリウム又はインジウム、Xはハロゲン、
aは2または3の整数をそれぞれ示す。)で表される化
合物又はその付加体である。
The organometallic compounds of aluminum, gallium and indium which are the subject of the present invention are represented by the general formula R a MX
3-a (wherein R is an alkyl group having 1 to 4 carbon atoms, M is aluminum, gallium or indium, X is halogen,
a represents an integer of 2 or 3. ) Is a compound or an adduct thereof.

【0012】具体的には、トリメチルアルミニウム、ト
リエチルアルミニウム、トリプロピルアルミニウム、ト
リブチルアルミニウム、トリメチルガリウム、トリエチ
ルガリウム、トリプロピルガリウム、トリブチルガリウ
ム、トリメチルインジウム、トリエチルインジウム、ト
リプロピルインジウム、トリブチルインジウム等のトリ
アルキル金属化合物、ジメチルアルミニウムクロライ
ド、ジエチルアルミニウムクロライド、ジメチルガリウ
ムクロライド、ジエチルガリウムクロライド、ジメチル
インジウムクロライド、ジエチルインジウムクロライド
等のアルキルハライド金属化合物、トリメチルアルミニ
ウム・ダイフォスフィン付加体、トリメチルガリウム・
ダイフォスフィン付加体、トリメチルインジウム・ダイ
フォスフィン付加体等のアルキル金属化合物の付加体等
が挙げられる。
Specifically, trialkyl such as trimethyl aluminum, triethyl aluminum, tripropyl aluminum, tributyl aluminum, trimethyl gallium, triethyl gallium, tripropyl gallium, tributyl gallium, trimethyl indium, triethyl indium, tripropyl indium, tributyl indium, etc. Metal compounds, alkyl halide metal compounds such as dimethyl aluminum chloride, diethyl aluminum chloride, dimethyl gallium chloride, diethyl gallium chloride, dimethyl indium chloride, diethyl indium chloride, trimethyl aluminum / dyphosphine adducts, trimethyl gallium /
Examples include adducts of alkyl metal compounds such as diphosphine adducts and trimethylindium / dyphosphine adducts.

【0013】[0013]

【実施例】以下図1の装置を用いた実施例により本発明
を説明する。
EXAMPLES The present invention will be described below with reference to examples using the apparatus of FIG.

【0014】(実施例1)内容積 300mlのガラス製の4
口フラスコを窒素ガスで置換後、n−ヘプタデカン 200
ml、粗トリメチルインジウム80gを仕込んだ。粗トリメ
チルインジウム中にはアルミ成分2000ppm 、シリコン成
分6ppm 、トルエン600ppm、ヘプタン1200ppm が含まれ
ていた。
(Example 1) 4 made of glass with an internal volume of 300 ml
After replacing the neck flask with nitrogen gas, n-heptadecane 200
ml and crude trimethylindium 80 g were charged. The crude trimethylindium contained aluminum component 2000 ppm, silicon component 6 ppm, toluene 600 ppm, and heptane 1200 ppm.

【0015】この容器を図1のように精製装置に取り付
けて、 140℃に加熱した。キャリアーガスとして窒素ガ
スを 200ml/min流した。キャリアーガスの出口に1Nの
硝酸50mlの入ったトラップを取り付けてキャリアーガス
中の低沸点有機金属不純物を捕集した。トラップは2時
間ごとに取り替えて捕集した金属不純物をICPで分析
した。さらにトラップを通ったキャリアーガスはガスク
ロマトグラフのFID検出器に導入して有機不純物を検
出した。有機不純物は4時間経過したところで検出され
なくなった。アルミとシリコンについてはそれぞれ18時
間、8時間経過したところで検出されなくなった。
This container was attached to a purifier as shown in FIG. 1 and heated to 140 ° C. Nitrogen gas was flowed at 200 ml / min as a carrier gas. A trap containing 50 ml of 1N nitric acid was attached to the carrier gas outlet to collect low-boiling organometallic impurities in the carrier gas. The trap was replaced every 2 hours and the collected metal impurities were analyzed by ICP. Further, the carrier gas passing through the trap was introduced into the FID detector of the gas chromatograph to detect organic impurities. Organic impurities were no longer detected after 4 hours. Aluminum and silicon were not detected after 18 hours and 8 hours, respectively.

【0016】すべての不純物が検出されなくなってか
ら、トリメチルインジウムを50torrで140 ℃まで加熱し
てn−ヘプタデカン中から留出分離させた。得られたト
リメチルインジウム中の不純物は、アルミ成分は0.2ppm
以下、シリコン成分は0.3ppm以下、トルエン、ヘプタン
はともに1ppm 以下であった。
After all impurities were not detected, trimethylindium was heated to 140 ° C. at 50 torr and distilled out from n-heptadecane. Impurities in the obtained trimethylindium were 0.2ppm in the aluminum component.
Below, the silicon content was 0.3 ppm or less, and both toluene and heptane were 1 ppm or less.

【0017】(実施例2)実施例1と同様の装置を用い
て、粗トリエチルインジウム80gとn−ヘプタデカン 2
00mlを 300mlの4口フラスコに仕込んで、 130℃に加熱
しキャリアーガスとして窒素ガスを 200ml/min流した。
粗トリエチルインジウム中にはアルミ成分 1300ppm、ト
ルエン 50ppm、ヘプタ子材料用の高純ン700ppmが含まれ
ていた。
(Example 2) Using the same apparatus as in Example 1, 80 g of crude triethylindium and n-heptadecane 2
00 ml was charged into a 300 ml four-necked flask, heated to 130 ° C., and nitrogen gas was flowed at 200 ml / min as a carrier gas.
The crude triethylindium contained 1300 ppm of aluminum component, 50 ppm of toluene, and 700 ppm of high purity for hepta child material.

【0018】有機不純物は4時間経過したところで検出
されなくなった。アルミは20時間経過したところで検出
されなくなった。
Organic impurities were no longer detected after 4 hours. Aluminum disappeared after 20 hours.

【0019】全ての不純物が検出されなくなってから、
トリエチルインジウムを5torrで105 ℃まで加熱してn
−ヘプタデカン中から留出分離させた。得られたトリエ
チルインジウム中の不純物は、アルミ成分が0.2ppm以
下、トルエン、ヘプタンはともに1ppm 以下であった。
After all impurities are no longer detected,
Heat triethylindium to 105 ° C at 5 torr and
-Distilled off from the heptadecane. Regarding the impurities in the obtained triethylindium, the aluminum component was 0.2 ppm or less, and both toluene and heptane were 1 ppm or less.

【0020】(実施例3)実施例1と同様にしてトリメ
チルアルミニウム・ダイフォスフィンの付加体を80g、
n−ヘプタデカンを 200mlを 300mlの4口フラスコに仕
込んで、 110℃で加熱しキャリアーガスの窒素ガスを 2
00ml/min流した。トリメチルアルミニウム・ダイフォス
フィン付加体中の不純物はシリコン4ppm 、ベンゼン70
0ppmであった。
Example 3 In the same manner as in Example 1, 80 g of an adduct of trimethylaluminum diphosphine,
200 ml of n-heptadecane was charged into a 300 ml four-necked flask and heated at 110 ° C, and nitrogen gas as a carrier gas was added.
Flowed at 00 ml / min. Impurities in the adduct of trimethylaluminum / diphosphine are silicon 4ppm, benzene 70
It was 0 ppm.

【0021】ベンゼンは4時間経過したところで検出さ
れなくなった。シリコンは6時間経過したところで検出
されなくなった。
Benzene was no longer detected after 4 hours. Silicon was not detected after 6 hours.

【0022】全ての不純物が検出されなくなってから、
トリメチルアルミニウム・ダイフォスフィン付加体を5
torrで 140℃まで加熱してトリメチルアルミニウムを留
出分離した。得られたトリメチルアルミニウム中の不純
物は、シリコンが0.3ppm以下、ベンゼンが1ppm 以下で
あった。
After all impurities are no longer detected,
Add trimethylaluminum / diphosphine adduct 5
Trimethylaluminum was distilled off and separated by heating to 140 ° C with a torr. Impurities in the obtained trimethylaluminum were 0.3 ppm or less for silicon and 1 ppm or less for benzene.

【0023】[0023]

【発明の効果】本発明によれば有機金属化合物中の低沸
点不純物を不活性なキャリアーガスを流すことで連続的
に除去できるようになった。さらに、キャリアーガス中
の不純物をモニターすることで、経験のないものでも効
率良く精製できるようになり電度有機金属化合物を製造
するのに頗る効果が大なるものである。
According to the present invention, the low boiling point impurities in the organometallic compound can be continuously removed by flowing an inert carrier gas. Furthermore, by monitoring the impurities in the carrier gas, even those with no experience can be efficiently purified, which is extremely effective in producing the electro-organic metal compound.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明で使用する精製装置の一例を示す説明図
である。
FIG. 1 is an explanatory diagram showing an example of a refining device used in the present invention.

【符号の説明】[Explanation of symbols]

1 流量計 2 4口フラスコ 3 攪拌機 4 マントルヒーター 5 硝酸トラップ 6 ガスクロマトグラムのFID検出器 7 テープヒーター 1 Flowmeter 2 4-necked flask 3 Stirrer 4 Mantle heater 5 Nitric acid trap 6 FID detector for gas chromatogram 7 Tape heater

【手続補正書】[Procedure amendment]

【提出日】平成4年12月15日[Submission date] December 15, 1992

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0023[Name of item to be corrected] 0023

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0023】[0023]

【発明の効果】本発明によれば有機金属化合物中の低沸
点不純物を不活性なキャリアーガスを流すことで連続的
に除去できるようになった。さらに、キャリアーガス中
の不純物をモニターすることで、経験のないものでも効
率良く精製できるようになり電子材料用の高純度有機金
属化合物を製造するのに頗る効果が大なるものである。
According to the present invention, the low boiling point impurities in the organometallic compound can be continuously removed by flowing an inert carrier gas. Furthermore, by monitoring the impurities in the carrier gas, even those with no experience can be efficiently purified, which is very effective in producing high-purity organometallic compounds for electronic materials.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 有機金属化合物を加熱し低沸点の不純物
を不活性なキャリアーガスを用いて除去し、このキャリ
アーガス中の不純物を経時的に測定することで精製状況
をモニターすることを特徴とする有機金属化合物の精製
方法。
1. The purification condition is monitored by heating an organometallic compound to remove impurities having a low boiling point using an inert carrier gas, and measuring impurities in the carrier gas with time. A method for purifying an organometallic compound.
【請求項2】 有機金属化合物が、一般式Ra MX3-a
(式中、Rは炭素数が1〜4のアルキル基、Mはアルミ
ニウム、ガリウム又はインジウム、Xはハロゲン、aは
2又は3の整数をそれぞれ示す。)で表されるもの又は
その付加体である請求項1記載の有機金属化合物の精製
方法。
2. The organometallic compound has the general formula R a MX 3-a.
(Wherein R is an alkyl group having 1 to 4 carbon atoms, M is aluminum, gallium or indium, X is halogen, and a is an integer of 2 or 3) or an adduct thereof. A method for purifying an organometallic compound according to claim 1.
JP32359592A 1992-11-09 1992-11-09 Purification method for organometallic compounds Expired - Fee Related JP3215195B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32359592A JP3215195B2 (en) 1992-11-09 1992-11-09 Purification method for organometallic compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32359592A JP3215195B2 (en) 1992-11-09 1992-11-09 Purification method for organometallic compounds

Publications (2)

Publication Number Publication Date
JPH06145177A true JPH06145177A (en) 1994-05-24
JP3215195B2 JP3215195B2 (en) 2001-10-02

Family

ID=18156468

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Country Status (1)

Country Link
JP (1) JP3215195B2 (en)

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EP1616872A2 (en) * 2004-06-18 2006-01-18 Shin-Etsu Chemical Co., Ltd. Purification method for organometallic compounds and organometallic compounds obtained therefrom
JP2008184419A (en) * 2007-01-30 2008-08-14 Ube Ind Ltd High-purity trialkylindium and its production method
JP2012062331A (en) * 2011-12-27 2012-03-29 Ube Industries Ltd High-purity trialkyl indium, and its production method
JP2016145170A (en) * 2015-02-09 2016-08-12 宇部興産株式会社 Method for producing solid organic metallic compound and production device therefor
CN118406074A (en) * 2024-07-03 2024-07-30 安徽亚格盛电子新材料股份有限公司 Purification method of crude trimethylaluminum product

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JP6108704B2 (en) 2011-07-13 2017-04-05 ダウ グローバル テクノロジーズ エルエルシー Organometallic compound purification
EP2559682B1 (en) 2011-08-15 2016-08-03 Rohm and Haas Electronic Materials LLC Organometallic compound preparation

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EP1616872A2 (en) * 2004-06-18 2006-01-18 Shin-Etsu Chemical Co., Ltd. Purification method for organometallic compounds and organometallic compounds obtained therefrom
EP1616872A3 (en) * 2004-06-18 2006-01-25 Shin-Etsu Chemical Co., Ltd. Purification method for organometallic compounds and organometallic compounds obtained therefrom
US7112691B2 (en) 2004-06-18 2006-09-26 Shin-Etsu Chemical Co., Ltd. Purification method for organometallic compounds and organometallic compounds obtained therefrom
KR100861207B1 (en) * 2004-06-18 2008-09-30 신에쓰 가가꾸 고교 가부시끼가이샤 Purification Method for Organometallic Compounds and Organometallic Compounds Obtained Therefrom
JP2008184419A (en) * 2007-01-30 2008-08-14 Ube Ind Ltd High-purity trialkylindium and its production method
JP2012062331A (en) * 2011-12-27 2012-03-29 Ube Industries Ltd High-purity trialkyl indium, and its production method
JP2016145170A (en) * 2015-02-09 2016-08-12 宇部興産株式会社 Method for producing solid organic metallic compound and production device therefor
CN118406074A (en) * 2024-07-03 2024-07-30 安徽亚格盛电子新材料股份有限公司 Purification method of crude trimethylaluminum product

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