JPS5940837B2 - Method for producing trialkyltin halide and monoalkyltin trihalide - Google Patents

Method for producing trialkyltin halide and monoalkyltin trihalide

Info

Publication number
JPS5940837B2
JPS5940837B2 JP4205376A JP4205376A JPS5940837B2 JP S5940837 B2 JPS5940837 B2 JP S5940837B2 JP 4205376 A JP4205376 A JP 4205376A JP 4205376 A JP4205376 A JP 4205376A JP S5940837 B2 JPS5940837 B2 JP S5940837B2
Authority
JP
Japan
Prior art keywords
halide
reaction
trialkyltin
monoalkyltin
producing
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
Application number
JP4205376A
Other languages
Japanese (ja)
Other versions
JPS52125130A (en
Inventor
秀之 今崎
勉 筒井
正澄 藤川
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.)
Nitto Kasei Co Ltd
Original Assignee
Nitto Kasei Co Ltd
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 Nitto Kasei Co Ltd filed Critical Nitto Kasei Co Ltd
Priority to JP4205376A priority Critical patent/JPS5940837B2/en
Publication of JPS52125130A publication Critical patent/JPS52125130A/en
Publication of JPS5940837B2 publication Critical patent/JPS5940837B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はトリアルキル錫ハライド及びモノアルキル錫ト
リハライドの製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a process for producing trialkyltin halides and monoalkyltin trihalides.

トリアルキル錫ハライドとくにトリブチル錫クロライド
は防ばい剤、殺菌剤、海中防汚用毒物及びその中間体と
して広く利用されている。
Trialkyltin halides, especially tributyltin chloride, are widely used as fungicides, fungicides, marine antifouling poisons, and intermediates thereof.

一方モノアルキル錫トリハライドとくにモノメチル錫、
モノブチル錫及びモノオクチル錫化合物は塩化ビニル樹
脂用安定剤の中間体として利用され、その需要は増大し
つつある。トリアルキル錫ハライドとモノアルキル錫ト
リハライドはそれぞれ別々の装置で別個の工程を経て製
造されているが、中でもモノアルキル錫ハライドの製造
は極めて困難で、得られたとしても工業的に不利な条件
下でかつ低収率にすぎない。
On the other hand, monoalkyltin trihalides, especially monomethyltin,
Monobutyltin and monooctyltin compounds are used as intermediates for stabilizers for vinyl chloride resins, and the demand for them is increasing. Trialkyltin halide and monoalkyltin trihalide are each produced through separate processes using separate equipment, but monoalkyltin halide is extremely difficult to produce, and even if it is obtained, it is produced under industrially unfavorable conditions. However, the yield is only low.

また従来からテトラアルキル錫に塩化第二錫をo℃附近
の低温で作用させ、次の反応式o℃ R4Sn+SnCl4−→R3SnCl+RSnCl3
(式中Rはアルキル基を示す)に従つてトリアルキル錫
クロライド及びモノアルキル錫トリクロライドを得る方
法があるが、低温であるために、温度制御が困難で、工
業的に不利である。
Furthermore, conventionally, tin chloride is applied to tetraalkyltin at a low temperature around 0°C, and the following reaction formula is obtained:
Although there is a method for obtaining trialkyltin chloride and monoalkyltin trichloride according to the formula (R represents an alkyl group), it is difficult to control the temperature because of the low temperature, which is industrially disadvantageous.

これ以上の温度例えば80℃で上記反応を行うと、今度
は上記生成物のほかにジアルキル錫シクロラードが約2
0%混入し、精製分離が困難であるばかりでなく、分解
や未反応物が残存するなど各生成物の収率が低下する欠
点がある。したがつて比較的低温(30〜180℃)で
上記反応を完全に進行させることは著しく困難であつた
。これらの欠点をなくすべく鋭意研究した結果、テトラ
アルキル錫とハロゲン化第二錫の反応をエーテル化合物
の存在下で行えば反応温度や両原料の仕込比に関係なく
、約1:1のモル比でしかも定量的にトリアルキル錫ハ
ライド及びモノアルキル錫トリハライドを製造できる方
法を見出した。
If the above reaction is carried out at a temperature higher than this, for example 80°C, then in addition to the above product, about 2 dialkyltin cyclolades will be produced.
0% contamination, which not only makes purification and separation difficult, but also has the disadvantage that the yield of each product decreases, such as decomposition and unreacted substances remaining. Therefore, it has been extremely difficult to allow the above reaction to proceed completely at a relatively low temperature (30 to 180°C). As a result of intensive research to eliminate these drawbacks, we found that if the reaction between tin tetraalkyl and tin halide is carried out in the presence of an ether compound, the molar ratio is about 1:1, regardless of the reaction temperature or the charging ratio of both raw materials. However, we have found a method that can quantitatively produce trialkyltin halides and monoalkyltin trihalides.

すなわち、本発明は、テトラヒドロフラン、ジオキサン
及びメトキシブタノールから選ばれるエーテル化合物の
存在下で、テトラアルキル錫とハロゲン化第二錫を反応
させトリアルキル錫ハライド及びモノアルキル錫トリハ
ライドを約1:1(モル比)の生成比で得ることを特徴
とするトリアルキル錫ハライド及びモノアルキル錫トリ
ハライドの製造法に関する。本発明方法において存在さ
せる添加物のエーテル化合物としてはとくに限定されな
いが、脂肪族エーテル及び脂環族エーテルが好ましい。
That is, the present invention involves reacting tetraalkyltin and stannic halide in the presence of an ether compound selected from tetrahydrofuran, dioxane, and methoxybutanol to prepare trialkyltin halide and monoalkyltin trihalide in a ratio of about 1:1 (mole). The present invention relates to a method for producing trialkyltin halides and monoalkyltin trihalides, characterized in that they are obtained at a production ratio of (ratio). The additive ether compound to be present in the method of the present invention is not particularly limited, but aliphatic ethers and alicyclic ethers are preferred.

例えばジエチルエーテル、ジプロピルエーテル、ジブチ
ルエーテル、エチルビニルエーテル、メトキシブタノー
ル、テトラヒドロフラン、ジオキサンなどがあげられる
。ハロゲン化第二錫と反応させるべきテトラアルキル錫
としては例えばテトラメチル錫、テトラエチル錫、テト
ラプロピル錫、テトラブチル錫、テトラアミル錫、テト
ラヘキシル錫、テトラシクロヘキシル錫、テトラオクチ
ル錫、テトラデシル錫、テトラドデシル錫などがあげら
れる。
Examples include diethyl ether, dipropyl ether, dibutyl ether, ethyl vinyl ether, methoxybutanol, tetrahydrofuran, and dioxane. Examples of the tetraalkyltin to be reacted with the stannic halide include tetramethyltin, tetraethyltin, tetrapropyltin, tetrabutyltin, tetraamyltin, tetrahexyltin, tetracyclohexyltin, tetraoctyltin, tetradecyltin, and tetradodecyltin. etc.

またハロゲン化第二錫としては四塩化錫、四臭化錫及び
四ヨウ化錫があげられる。本発明方法において添加され
るエーテル化合物の添加量は通常ハロゲン化第二錫に対
して2倍モル以上あれば十分であり、溶媒の代りにこれ
以上、例えば4倍モル以上使用してもよい。
Examples of the stannic halides include tin tetrachloride, tin tetrabromide, and tin tetraiodide. The amount of the ether compound added in the method of the present invention is normally sufficient if it is at least 2 times the molar amount of the stannic halide, and it may be used in place of the solvent, for example, at least 4 times the molar amount.

本発明方法はエーテル化合物の存在下で行われるが、そ
のほかに必要に応じて不活性溶媒例えばベンゼン、トル
エン、キシレン、シクロヘキサン、n−ヘキサンなどを
使用してもよい。
Although the method of the present invention is carried out in the presence of an ether compound, an inert solvent such as benzene, toluene, xylene, cyclohexane, n-hexane, etc. may be used if necessary.

反応温度はとくに制限されないが工業的に有利な温度例
えば30〜180℃の範囲内で行うことができる。
Although the reaction temperature is not particularly limited, it can be carried out at an industrially advantageous temperature, for example, within the range of 30 to 180°C.

反応を円滑に行うため添加物又は溶媒の還流温度で行な
つてもよい。反応は通常1〜2時間で終了する。本発明
方法は一般に次のようにして実施される。
In order to carry out the reaction smoothly, it may be carried out at the reflux temperature of the additive or solvent. The reaction usually completes in 1 to 2 hours. The method of the present invention is generally carried out as follows.

まずハロゲン化第二錫を反応容器に仕込み、これにあま
り激しく発熱しない程度のスピードでエーテル化合物の
添加物を滴下し、付加物を生成させる。次いでこの付加
物にテトラアルキル錫を加えて加熱し、反応を完了させ
る。反応後、過剰のハロゲン化第二錫があれば、これは
添加物と付加物を作り沈澱するので沢去する。反応混合
物を濃縮し、添加物(及び溶媒)を留去した後、減圧又
は常圧で分留し、トリアルキル錫ハライドとモノアルキ
ル錫トリハライドを得る。モノアルキル錫トリハライド
の親永性を利用して水で抽出分離することもできる。本
発明方法によればトリアルキル錫ハライドとモノアルキ
ル錫トリハライドをモル比で約1:1の割合で生ずる。
First, stannic halide is charged into a reaction vessel, and an ether compound additive is added dropwise to the reaction vessel at a speed that does not generate too much heat to form an adduct. The tetraalkyltin is then added to the adduct and heated to complete the reaction. After the reaction, if there is an excess of stannic halide, it forms additives and adducts and precipitates out, so it is washed away. After concentrating the reaction mixture and distilling off the additives (and solvent), fractional distillation is carried out under reduced pressure or normal pressure to obtain trialkyltin halide and monoalkyltin trihalide. It is also possible to extract and separate with water by taking advantage of the philic nature of monoalkyltin trihalide. The process of the present invention produces trialkyltin halide and monoalkyltin trihalide in a molar ratio of about 1:1.

この割合はハロゲン化第二錫を過剰に使用しても変らな
い。またジアルキル錫ジハライドの副生は実質土認めら
れない。さらに原料のテトラアルキル錫にトリアルキル
錫ハライドを含むことがあるが、本発明方法には何ら影
響を与えず、その分だけ生成物のトリアルキル錫ハライ
ドを増加させるにすぎない。本発明方法によつてトリア
ルキル錫ハライドとモノアルキル錫トリハライドを同時
に製造できると共に、精製分離が容易であるから、従来
の方法に見られない工業的に有利な方法である。次に本
発明方法を説明するために実施例を掲げる。
This ratio does not change even if the stannic halide is used in excess. In addition, virtually no by-product of dialkyltin dihalide was observed. Furthermore, although the raw material tetraalkyltin may contain trialkyltin halide, it does not affect the process of the present invention, but only increases the trialkyltin halide in the product by that amount. By the method of the present invention, trialkyltin halide and monoalkyltin trihalide can be produced simultaneously, and purification and separation is easy, so it is an industrially advantageous method that is not found in conventional methods. Examples will now be given to explain the method of the present invention.

実施例 1 攪拌器、温度計、冷却器及び滴下漏斗を備えた11の四
つロフラスコに四塩化錫1307(0.5モル)とベン
ゼン200m1を仕込み、撹拌しながら、滴下漏斗より
テトラヒドロフラン86.17(1モル)を室温にて滴
下する。
Example 1 1307 (0.5 mol) of tin tetrachloride and 200 ml of benzene were charged into 11 four-bottle flasks equipped with a stirrer, a thermometer, a condenser, and a dropping funnel, and while stirring, 86.17 g of tetrahydrofuran was added from the dropping funnel. (1 mol) is added dropwise at room temperature.

四塩化錫とテトラヒドロフランは直ちに反応し発熱する
ので、冷却することによりコントロールする。滴下完了
後加熱し還流下に30分間反応を行う。ついで還流温度
下(約80℃)でテトラブチル錫173.6y(0,5
モル)を30分間で滴下し、その後1時間反応を行う。
反応混合物は淡褐色透明溶液である。この反応混合液を
ガスクロマトグラフイ一にて生成物の組成分析した結果
モノブチル錫トリクロライドとトリブチル錫クロライド
のピークのみが見られ、未反応四塩化錫、テトラブチル
錫及びジブチル錫シクロラードは痕跡程度であつた。モ
ノブチル錫トワクロライドとトワブチル錫クロライドの
生成比はモル比で約1:1(重量比で46:54)であ
つた。反応混合物を濃縮しベンゼン及びテトラヒドロフ
ランを留去した後、減圧蒸留し、92〜94゜C/10
mmH7の留分のモノブチル錫トリクロライド140.
07(純度99.2%)及び144〜146℃/10m
711H7の留分のトリブチル錫クロライド160.9
y(純度98.7%)を得た。合計収率99.1%。実
施例 2〜6 実施例1において同じ量の四塩化錫、テトラブチル錫及
びベンゼンを用い、テトラヒドロフランの添加量を変化
させ、同反応操作を行なつた。
Tin tetrachloride and tetrahydrofuran react immediately and generate heat, so the reaction is controlled by cooling. After the dropwise addition is completed, the mixture is heated and reacted under reflux for 30 minutes. Then, 173.6y (0,5
mol) was added dropwise over 30 minutes, and the reaction was then carried out for 1 hour.
The reaction mixture is a light brown clear solution. As a result of analyzing the product composition of this reaction mixture using gas chromatography, only peaks for monobutyltin trichloride and tributyltin chloride were observed, and only traces of unreacted tin tetrachloride, tetrabutyltin, and dibutyltin cyclolade were observed. Ta. The production ratio of monobutyltin towachloride and towabutyltin chloride was approximately 1:1 in molar ratio (46:54 in weight ratio). The reaction mixture was concentrated to remove benzene and tetrahydrofuran, and then distilled under reduced pressure to 92-94°C/10
Monobutyltin trichloride of mmH7 fraction 140.
07 (purity 99.2%) and 144-146℃/10m
Tributyltin chloride of fraction 711H7 160.9
y (purity 98.7%) was obtained. Total yield 99.1%. Examples 2 to 6 The same reaction operations as in Example 1 were carried out using the same amounts of tin tetrachloride, tetrabutyltin and benzene, but varying the amount of tetrahydrofuran added.

結果を第1表に示した。実施例 7〜9 本実施例ではテトラブチル錫104.17(0.3モル
)、ベンゼン200m1を用い、四塩化錫の仕込割合を
変えた。
The results are shown in Table 1. Examples 7 to 9 In this example, 104.17 (0.3 mol) of tetrabutyltin and 200 ml of benzene were used, and the charging ratio of tin tetrachloride was changed.

テトラヒドロフランの添加量を 闘四塩化錫に対して2
倍モル量を用いるほかは実施★冫例1と同じ条件、操作
で反応を行なつた。なお本実施例では過剰の四塩化錫を
用いるため、反応後テトラヒト狛フランとの付加物とし
て沈澱する。この沈澱物を沢過してその量を計つた。結
果を第2表に示した。実施例 10 反応容器に四塩化錫130.07(0.5モル)を仕込
み、これにメトキシブタノール114.2y(1.5モ
ル)を室温にて約30分間で滴下した。
The amount of tetrahydrofuran added is 2 to tin tetrachloride.
The reaction was carried out under the same conditions and operations as in Example 1 except that twice the molar amount was used. In this example, since an excess of tin tetrachloride is used, it precipitates as an adduct with tetrahydrofuran after the reaction. This precipitate was filtered out and its amount was measured. The results are shown in Table 2. Example 10 A reaction vessel was charged with 130.07 y (0.5 mol) of tin tetrachloride, and 114.2 y (1.5 mol) of methoxybutanol was added dropwise thereto over about 30 minutes at room temperature.

その後100±5℃の温度に30分間保ち、130±5
℃に加熱して、約1時間でテトラオクチル錫267.8
7(0.5モル)を滴下した.さらにこの温度で1時間
反応させた。得られた反応混合物を濃縮しガスクロマト
グラフイ一にて生成物の組成を調べたところモノオクチ
ル錫トリクロライドとトリオクチル錫モノクロライドが
重量比40.3:59.7(モル比1:1)で存在し、
ジオクチル錫シクロラードは痕跡しか認められなかつた
。四塩化錫及びテトラオクチル錫のピークは認められな
かつた。反応混合物に10%塩酸水300m1を加えて
モノオクチル錫トリクロライドを抽出し、塩酸水抽出層
を苛性ソーダ水溶液にて加水分解し、モノオクチル錫酸
を130.87得た(メチル化法により純度を分析した
結果99.1%であつた)。有機層は活性白土を加えて
脱水、脱色し、▲過後の▲液を濃縮するとトリオクチル
錫クロライドが236.5y(純度98.7%)得られ
た。合計収率はほぼ定量的であつた。実施例 11 反応容器に四塩化錫130.0y(0.5モル)とトル
エン200m2を仕込み、これにジオキサン88.1y
(1.0モル)を室温にて約30分間で滴下した。
After that, keep it at a temperature of 100±5℃ for 30 minutes, and then
℃ and in about 1 hour, 267.8% of tetraoctyltin
7 (0.5 mol) was added dropwise. The reaction was further continued at this temperature for 1 hour. The resulting reaction mixture was concentrated and the composition of the product was examined using gas chromatography, and it was found that the weight ratio of monooctyltin trichloride and trioctyltin monochloride was 40.3:59.7 (molar ratio 1:1). exists,
Only traces of dioctyltincyclolade were observed. No peaks for tin tetrachloride or tetraoctyltin were observed. 300 ml of 10% hydrochloric acid water was added to the reaction mixture to extract monooctyltin trichloride, and the hydrochloric acid water extract layer was hydrolyzed with an aqueous caustic soda solution to obtain 130.87% monooctyltin trichloride (purity was determined by the methylation method). The analysis result was 99.1%). The organic layer was dehydrated and decolorized by adding activated clay, and the resulting solution was concentrated to obtain 236.5y of trioctyltin chloride (purity 98.7%). The total yield was almost quantitative. Example 11 A reaction vessel was charged with 130.0 y (0.5 mol) of tin tetrachloride and 200 m2 of toluene, and 88.1 y of dioxane was added thereto.
(1.0 mol) was added dropwise at room temperature over about 30 minutes.

ついで100±5℃の温度に15分間保つた後、100
±5℃の温度にてテトラプロピル錫145.57(0.
5モル)を45分間で滴下した。さらに同温度で15分
間保つた。得られた反応混合物を濃縮しガスクロマトグ
ラフイ一にて生成物の組成を調べたところモノプロピル
錫トリクロライドとトリプロピル錫クロライドの生成比
が重量比48.6:51.4(モル比で約1:1)であ
つた。またジプロピル錫シクロラードは痕跡しか認めら
れなかつた。四塩化錫及びテトラプロピル錫のピークは
全く認められなかつた。反応混合物を蒸留して、モノプ
ロピル錫トリクロライド131.87(B.p.99〜
100℃/13龍Hg)とトリプロピル錫クロライド1
38.7y(B.p.l22〜123℃/13m77H
g)を得た。
Then, after keeping the temperature at 100±5℃ for 15 minutes,
Tetrapropyltin 145.57 (0.
5 mol) was added dropwise over 45 minutes. It was further kept at the same temperature for 15 minutes. The resulting reaction mixture was concentrated and the composition of the product was examined using gas chromatography. The production ratio of monopropyltin trichloride and tripropyltin chloride was 48.6:51.4 by weight (about a molar ratio). 1:1). Also, only traces of dipropyltin cyclolade were observed. No peaks of tin tetrachloride and tin tetrapropyl were observed. The reaction mixture was distilled to give monopropyltin trichloride 131.87 (B.p. 99~
100℃/13 Dragon Hg) and tripropyltin chloride 1
38.7y (B.p.l22~123℃/13m77H
g) was obtained.

Claims (1)

【特許請求の範囲】[Claims] 1 テトラヒドロフラン、ジオキサン及びメトキシブタ
ノールから選ばれるエーテル化合物の存在下で、テトラ
アルキル錫とハロゲン化第二錫を反応させトリアルキル
錫ハライド及びモノアルキル錫トリハライドを約1:1
(モル比)の生成比で得ることを特徴とするトリアルキ
ル錫ハライド及びモノアルキル錫トリハライドの製造法
1 In the presence of an ether compound selected from tetrahydrofuran, dioxane, and methoxybutanol, tetraalkyltin and stannic halide are reacted to form trialkyltin halide and monoalkyltin trihalide at a ratio of approximately 1:1.
A method for producing trialkyltin halide and monoalkyltin trihalide, characterized in that they are obtained at a production ratio of (molar ratio).
JP4205376A 1976-04-13 1976-04-13 Method for producing trialkyltin halide and monoalkyltin trihalide Expired JPS5940837B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4205376A JPS5940837B2 (en) 1976-04-13 1976-04-13 Method for producing trialkyltin halide and monoalkyltin trihalide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4205376A JPS5940837B2 (en) 1976-04-13 1976-04-13 Method for producing trialkyltin halide and monoalkyltin trihalide

Publications (2)

Publication Number Publication Date
JPS52125130A JPS52125130A (en) 1977-10-20
JPS5940837B2 true JPS5940837B2 (en) 1984-10-03

Family

ID=12625358

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JP4205376A Expired JPS5940837B2 (en) 1976-04-13 1976-04-13 Method for producing trialkyltin halide and monoalkyltin trihalide

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JPS52125130A (en) 1977-10-20

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