JPH04308595A - Production of mono-exchanger compound in organosilicone compound - Google Patents

Production of mono-exchanger compound in organosilicone compound

Info

Publication number
JPH04308595A
JPH04308595A JP10196291A JP10196291A JPH04308595A JP H04308595 A JPH04308595 A JP H04308595A JP 10196291 A JP10196291 A JP 10196291A JP 10196291 A JP10196291 A JP 10196291A JP H04308595 A JPH04308595 A JP H04308595A
Authority
JP
Japan
Prior art keywords
compound
exchanger
formula
mono
expressed
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.)
Withdrawn
Application number
JP10196291A
Other languages
Japanese (ja)
Inventor
Tsunemasa Ueno
上野 恒正
Shigefumi Kuramoto
成史 倉本
Taisei Fuku
大成 富久
Tadahiro Yoneda
忠弘 米田
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.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai 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 Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP10196291A priority Critical patent/JPH04308595A/en
Publication of JPH04308595A publication Critical patent/JPH04308595A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the subject mono-exchanger compound in high yield by reacting an alkoxysilane with a hydroxy compound and then separating poly- exchanger by-products from the mono-exchanger compound and recycling the poly-exchanger by-products to the reaction system. CONSTITUTION:When a compound (e.g. tetramethoxysilane) expressed by formula I (R<1> is <=10C hydrocarbon residue; R<2> is H or <=5 C alkyl or <=5C acyl; (n) is 0, 1 or 2) is made to react with a compound (e.g. 2-hydroxyethyl methacrylate) expressed by the formula R<3>-OH (R<3> is <=20C organic residue) to produce a mono-exchanger compound (e.g. methacryloxyethoxytrimethoxysilane) expressed by formula II, the mono- exchanger compond expressed by formula II is separated from poly-exchanger by-products such as di-exchanger compound expressed by formula III or tri- exchanger compound expressed by formula IV, and the separated and eliminated poly-exchanger by-products are mixed into a reaction system and subjected to exchange reaction to provide the objective mono-exchanger compound expressed by formula II in high yield.

Description

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

【0001】0001

【産業上の利用分野】本発明は有機珪素化合物における
交換反応を制御して、目的とするモノ交換体化合物を高
収率に製造することのできる方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a desired monoexchanger compound in high yield by controlling the exchange reaction in an organosilicon compound.

【0002】0002

【従来の技術】有機珪素化合物、特にアルコキシ基やア
シルオキシ基を有する有機珪素化合物を、ヒドロキシル
基含有化合物やカルボキシル基含有化合物との交換反応
に付すにあたっては、次式に示す様な多段階の逐次平衡
反応を起こすことが知られており、目的とするモノ交換
体化合物を高収率に得ることは困難である。
[Prior Art] When subjecting an organosilicon compound, especially an organosilicon compound having an alkoxy group or an acyloxy group, to an exchange reaction with a hydroxyl group-containing compound or a carboxyl group-containing compound, a multi-step sequential reaction is carried out as shown in the following formula. It is known that an equilibrium reaction occurs, making it difficult to obtain the desired monoexchanger compound in high yield.

【0003】0003

【化5】[C5]

【0004】(式中R1は炭素数10以下の炭化水素残
基、R2は水素原子、または炭素数5以下のアルキル基
または炭素数5以下のアシル基、R3は炭素数20以下
の有機残基、nは0,1または2を夫々意味する)
(In the formula, R1 is a hydrocarbon residue having 10 or less carbon atoms, R2 is a hydrogen atom, an alkyl group having 5 or less carbon atoms, or an acyl group having 5 or less carbon atoms, and R3 is an organic residue having 20 or less carbon atoms. , n means 0, 1 or 2 respectively)

【0
005】即ち上記平衡式で示す様に、反応生成物中には
モノ交換体化合物(A) の他に、ジ交換体化合物(B
) やトリ交換体化合物(C) などの多交換体化合物
が混在しており、従ってモノ交換体化合物(A) の収
率は低くならざるを得ない。
0
That is, as shown in the above equilibrium equation, the reaction product contains not only the monoexchanger compound (A) but also the diexchanger compound (B).
) and tri-exchanger compound (C), and therefore the yield of mono-exchanger compound (A) must be low.

【0006】この様な反応の典型例としては、例えばJ
.Am.Chem.Soc.,1946 (68) 7
3 に記載されているテトラエトキシシランとアリルア
ルコールの反応が公知であり、これによれば4つのエト
キシ基のうち1つがアリルオキシ基に交換されたモノ交
換体の他、エトキシ基のうち2つがアリルオキシ基に交
換されたジ交換体、エトキシ基のうち3つがアリルオキ
シ基に交換されたトリ交換体、並びに全てのエトキシ基
がアリルオキシ基に交換されたテトラ交換体が全て生成
して反応系中に混在し、従ってモノ交換体の収率が非常
に低くなる旨報告されている。
A typical example of such a reaction is, for example, J
.. Am. Chem. Soc. , 1946 (68) 7
The reaction between tetraethoxysilane and allyl alcohol described in 3 is known, and according to this, in addition to a monoexchanged product in which one of the four ethoxy groups is replaced with an allyloxy group, two of the ethoxy groups are replaced with an allyloxy group. A di-exchanger in which three ethoxy groups are exchanged with allyloxy groups, a tri-exchanger in which three of the ethoxy groups are exchanged with allyloxy groups, and a tetra-exchanger in which all ethoxy groups are exchanged with allyloxy groups are all produced and mixed in the reaction system. However, it has been reported that the yield of the monoexchanger is therefore very low.

【0007】しかるにこれらのモノ交換体は例えばゾル
ーゲル反応等によって各種機能性材料を製造するときの
原料として有用である他、反応性基を有することにより
各種機能性高分子製造用モノマーとしても有用であり、
モノ交換体を高収率で製造することのできる手段を確立
することが望まれている。
However, these monoexchangers are not only useful as raw materials for producing various functional materials through sol-gel reactions, but also as monomers for producing various functional polymers because of their reactive groups. can be,
It is desired to establish a means by which monoexchangers can be produced in high yields.

【0008】[0008]

【発明が解決しようとする課題】本発明は上記の様な事
情に注目してなされたものであって、モノ交換体化合物
を高収率で製造することのできる方法を提供しようとす
るものである。
[Problems to be Solved by the Invention] The present invention has been made in view of the above-mentioned circumstances, and it is an object of the present invention to provide a method that can produce a monoexchanger compound in high yield. be.

【0009】[0009]

【課題を解決するための手段】上記目的を達成すること
のできた本発明の製造方法とは、一般式
[Means for Solving the Problems] The manufacturing method of the present invention that can achieve the above object is based on the general formula

【0010】0010

【化6】[C6]

【0011】(式中R1,R2,nは夫々前と同じ意味
)で示される化合物(A)に、一般式 R3−OH                    
            (B)(式中R3は前と同じ
意味)で示される化合物(B)を反応させることによっ
て生成する生成物のうち、一般式
(wherein R1, R2, n each have the same meanings as before), a compound (A) of the general formula R3-OH
(B) Among the products produced by reacting the compound (B) (in which R3 has the same meaning as before), the general formula

【0012】0012

【化7】[C7]

【0013】で示されるモノ交換体化合物(C)を、一
般式
The monoexchanger compound (C) represented by the general formula

【0014】[0014]

【化8】[Chemical formula 8]

【0015】で示されるジ交換体化合物(D)や、一般
The di-exchanger compound (D) represented by

【0016】[0016]

【化9】[Chemical formula 9]

【0017】で示されるトリ交換体化合物(E)等の多
交換体副生物から分離採取すると共に、分離除去された
前記多交換体副生物を前記化合物(A)と化合物(B)
の反応系に添加することを要旨とするものである。従っ
て多交換体副生物は反応生成物から分離して循環的に反
応原料として再使用されることになり、モノ交換体化合
物(C)から多交換体副生物への平衡移動を抑制し、そ
の結果としてモノ交換体化合物(C)の収率向上が達成
されたのである。
The multi-exchanger by-products such as the tri-exchanger compound (E) shown below are separated and collected, and the separated and removed multi-exchanger by-products are combined with the compound (A) and compound (B).
The gist of this is that it is added to the reaction system. Therefore, the multi-exchanger by-product is separated from the reaction product and cyclically reused as a reaction raw material, suppressing the equilibrium shift from the mono-exchanger compound (C) to the multi-exchanger by-product, and As a result, an improvement in the yield of the monoexchanger compound (C) was achieved.

【0018】[0018]

【発明の構成の説明】以下本発明を更に詳述するが、説
明の便宜から、 第1工程 化合物(A)、化合物(B)および第2工程からリサイ
クルされる多交換体副生物を反応させてモノ交換体化合
物(C)、並びに多交換体副生物からなる混合物を製造
するステップ、
DESCRIPTION OF THE STRUCTURE OF THE INVENTION The present invention will be described in more detail below, but for convenience of explanation, the first step compound (A), the compound (B), and the multi-exchanger by-product recycled from the second step will be reacted. producing a mixture consisting of a mono-exchanger compound (C) and a multi-exchanger by-product;

【0019】第2工程 第1工程で得られた混合物からモノ交換体化合物(C)
を分離採取するとともに、残りの多交換体副生物を第1
工程にリサイクルするステップ、の2工程に分けて述べ
ることとする。
Second step Mono exchanger compound (C) is extracted from the mixture obtained in the first step.
At the same time, the remaining multi-exchanger by-products are collected in the first
This will be explained in two steps: the recycling step.

【0020】第1工程で生成するのはモノ交換体化合物
(C) と多交換体副生物(D),(E),…の混合物
であり、これらの中からモノ交換体化合物(C) を目
的物質として分離する。分離手段は一切制限されず、化
合物(C) におけるR1,R2,R3,nの種類に応
じて最適の手段を採用すれば良い。代表的な手段として
は、蒸留、クロマトグラフィー、再結晶、抽出等の方法
が例示される。モノ交換体化合物(C) が分離された
後の多交換体副生物(D),(E),…を含む混合物、
或は、必要により個別に分離されたジ交換体化合物(D
) やトリ交換体化合物(E) 等はこれらを精製する
ことなくそのままリサイクルし、化合物(A) と化合
物(B) の反応系に添加して交換反応を行なわせる。 多交換体副生物は化合物(A) ,化合物(B) と混
合して反応系に添加しても、化合物(A) ,化合物(
B) と別々に添加してもよい。第1工程と第2工程は
バッチ的に分離して行うこともできるが、回分操作的に
連続して行なうことも可能である。
What is produced in the first step is a mixture of the mono-exchanger compound (C) and the multi-exchanger by-products (D), (E), etc., from which the mono-exchanger compound (C) is extracted. Separate as target substance. The separation means is not limited at all, and an optimal means may be adopted depending on the types of R1, R2, R3, and n in compound (C). Typical methods include methods such as distillation, chromatography, recrystallization, and extraction. A mixture containing polyexchanger by-products (D), (E), ... after the monoexchanger compound (C) is separated,
Alternatively, di-exchanger compounds (D
), the tri-exchanger compound (E), etc. are recycled as they are without purification, and added to the reaction system of compound (A) and compound (B) to carry out the exchange reaction. Even if the multi-exchanger by-product is mixed with compound (A) and compound (B) and added to the reaction system, compound (A) and compound (
B) may be added separately. The first step and the second step can be carried out separately in a batchwise manner, but they can also be carried out continuously in a batchwise manner.

【0021】上記第1工程においては、上記反応が既述
の如く逐次的且つ可逆的であることにより、反応系内に
おいて不均化反応を起こす。従って原料化合物(A) 
および(B) 、並びにリサイクルされる多交換体副生
物(D),(E),…等のモル比に応じた反応制御が行
なわれることとなり、特に化合物(A),(B) の量
を適当に選べば、第1工程における反応生成物中の各交
換体化合物(C),(D),(E),…の組成比を任意
の値に、且つ再現性良く制御することが可能となる。こ
こで原料化合物(A),(B) の量は第2工程からリ
サイクルされる多交換体副生物混合体における各交換体
化合物(D),(E),…の組成を考慮して定めること
が推奨される。尚第1工程における反応原料中の総Si
モル数と総OR3基モル数の比は、(0.1:1) 〜
(20:1)、好ましくは(1:1) 〜(10:1)
の範囲から選定すれば良い。
In the first step, since the reaction is sequential and reversible as described above, a disproportionation reaction occurs within the reaction system. Therefore, the raw material compound (A)
and (B), and the recycled multi-exchanger by-products (D), (E), etc. The reaction will be controlled according to the molar ratio of the compounds (A), (B), etc. If selected appropriately, it is possible to control the composition ratio of each exchanger compound (C), (D), (E), ... in the reaction product in the first step to any value and with good reproducibility. Become. Here, the amounts of the raw material compounds (A) and (B) should be determined by considering the composition of each exchanger compound (D), (E), ... in the multi-exchanger byproduct mixture recycled from the second step. is recommended. In addition, the total Si in the reaction raw materials in the first step
The ratio of the number of moles to the total number of moles of OR3 groups is (0.1:1) ~
(20:1), preferably (1:1) to (10:1)
You can choose from the range.

【0022】次に本発明で用いられるR1、R2および
R3の定義について説明する。R1で示される炭素数1
0以下の炭化水素残基としては、直鎖状または分岐状の
飽和もしくは不飽和アルキル基(例えばメチル,エチル
,プロピル,イソプロピル,ブチル,第2級ブチル,第
3級ブチル,ペンチル,イソペンチル,ヘキシル,ヘプ
チル,2−メチルヘキシル,3−メチルヘキシル,オク
チル,ノニル,デシル,ビニル,1−メチルビニル,ア
リール等)、芳香族残基(例えばフェニル,トリル,キ
シリル,ナフチル等),脂環式アルキル基(例えばシク
ロプロピル,シクロペンチル,シクロヘキシル,4−メ
チルシクロヘキシル等)が示される。
Next, the definitions of R1, R2 and R3 used in the present invention will be explained. Carbon number 1 represented by R1
Zero or less hydrocarbon residues include linear or branched saturated or unsaturated alkyl groups (e.g. methyl, ethyl, propyl, isopropyl, butyl, secondary butyl, tertiary butyl, pentyl, isopentyl, hexyl). , heptyl, 2-methylhexyl, 3-methylhexyl, octyl, nonyl, decyl, vinyl, 1-methylvinyl, aryl, etc.), aromatic residues (e.g. phenyl, tolyl, xylyl, naphthyl, etc.), alicyclic alkyl Groups such as cyclopropyl, cyclopentyl, cyclohexyl, 4-methylcyclohexyl, etc. are indicated.

【0023】R2で示される炭素数5以下のアルキル基
としては、メチル,エチル,プロピル,イソプロピル,
ブチル,第2級ブチル,第3級ブチル,ペンチル等の直
鎖状または分岐状アルキル基が例示される。また炭素数
5以下のアシル基としてはアセチル,プロピオニル,ブ
チリル,エトキシカルボニル,プロポキシカルボニル等
が例示される。従ってOR2基としては、メトキシ,エ
トキシ,プロポキシ,ブトキシ等のアルコキシ基、或は
アセチルオキシ,プロピオニルオキシ,エトキシカルボ
ニルオキシ等のアシルオキシ基が得られる。
The alkyl group having 5 or less carbon atoms represented by R2 includes methyl, ethyl, propyl, isopropyl,
Straight chain or branched alkyl groups such as butyl, secondary butyl, tertiary butyl, pentyl and the like are exemplified. Examples of the acyl group having 5 or less carbon atoms include acetyl, propionyl, butyryl, ethoxycarbonyl, propoxycarbonyl, and the like. Therefore, as the OR2 group, an alkoxy group such as methoxy, ethoxy, propoxy, butoxy, or an acyloxy group such as acetyloxy, propionyloxy, ethoxycarbonyloxy, etc. can be obtained.

【0024】R3で示される炭素数20以下の有機残基
とは、反応性2重結合(例えばビニル,アクリロイル,
メタクリロイル等),エポキシ基,カルボニル基,カル
バモイル基,オキサゾリン骨格,直鎖状または分岐状ア
ルキル基,脂環式炭化水素基,芳香族炭化水素基等を有
する有機残基を意味し、R3−OHとして示される化合
物はアルコール類,フェノール類またはカルボン酸類で
ある。
The organic residue having 20 or less carbon atoms represented by R3 is a reactive double bond (such as vinyl, acryloyl,
R3-OH Compounds shown as are alcohols, phenols, or carboxylic acids.

【0025】上記各種定義で例示された様な基を有する
化合物を例示すると、まず化合物(A) としては、テ
トラメトキシシラン,テトラエトキシシラン,テトライ
ソプロポキシシラン,テトラブトキシシラン,メチルト
リメトキシシラン,メチルトリエトキシシラン,フェニ
ルトリメトキシシラン,フェニルトリエトキシシラン,
ジメチルジメトキシシラン,ジメチルジエトキシシラン
,ジフェニルジメトキシシラン,ジフェニルジエトキシ
シラン等のアルコキシシラン化合物;テトラアセトキシ
シラン,メチルトリアセトキシシラン,ジメチルジアセ
トキシシラン,フェニルトリアセトキシシラン等のアシ
ロキシシラン化合物;ジフェニルシランジオール等のシ
ラノール化合物等を挙げることができる。
[0025] Examples of compounds having groups as exemplified in the various definitions above include compound (A) such as tetramethoxysilane, tetraethoxysilane, tetraisopropoxysilane, tetrabutoxysilane, methyltrimethoxysilane, Methyltriethoxysilane, phenyltrimethoxysilane, phenyltriethoxysilane,
Alkoxysilane compounds such as dimethyldimethoxysilane, dimethyldiethoxysilane, diphenyldimethoxysilane, diphenyldiethoxysilane; acyloxysilane compounds such as tetraacetoxysilane, methyltriacetoxysilane, dimethyldiacetoxysilane, phenyltriacetoxysilane; diphenylsilane Examples include silanol compounds such as diols.

【0026】次に化合物(B) としては、例えばNext, as the compound (B), for example,

【0
027】
0
027]

【化10】[Chemical formula 10]

【0028】(式中R4は炭素数1〜10のアルキレン
基またはオキシアルキレン基,R5は水素原子またはメ
チル基を示す)等が例示される。ここでアルキレン基と
してはエチレン,トリメチレン,テトラメチレン,ペン
タメチレン,ヘキサメチレン,ヘプタメチレン,オクタ
メチレン,ノナメチレン,デカメチレン,プロピレン,
エチルエチレン,2−メチルテトラメチレン,3−メチ
ルテトラメチレン等の直鎖状または分岐状アルキレン基
が例示され、またオキシアルキレン基としては、上記の
様に例示されたアルキレン基における炭素鎖が任意の位
置で酸素原子で中断された基が例示される。
Examples include (in the formula, R4 represents an alkylene group or oxyalkylene group having 1 to 10 carbon atoms, and R5 represents a hydrogen atom or a methyl group). Here, the alkylene groups include ethylene, trimethylene, tetramethylene, pentamethylene, hexamethylene, heptamethylene, octamethylene, nonamethylene, decamethylene, propylene,
Examples include linear or branched alkylene groups such as ethylethylene, 2-methyltetramethylene, and 3-methyltetramethylene, and examples of oxyalkylene groups include those in which the carbon chain in the alkylene group exemplified above is arbitrary. An example is a group interrupted by an oxygen atom at a position.

【0029】上記の様な化合物(F) 〜(M) につ
いてこれを更に具体例をもって説明すれば下記の通りで
ある。 CH3=C(CH3)−COOCH2CH2OHCH2
=C(CH3)−COOCH2CH2CH2OHCH2
=C(CH3)−COOCH2CH(CH3)OHCH
2=C(CH3)−COOCH2CH2CH2CH2O
HCH2=C(CH3)−COOCH2CH2OCH2
CH2OH CH2=CH−COOCH2CH(CH3)OHCH2
=CH−COOCH2CH2CH2CH2OHCH2=
CH−CH2OH CH2=CH−CH2CH2OCH2CH2OHCH2
=C(CH3)−CONHCH2CH2OHCH2=C
H−CONHCH2CH2OHCH2=C(CH3)−
COOH CH2=CH−COOH CH2=C(CH3)−CONHCH2COOHCH2
=CH−CH2−COOH
The above compounds (F) to (M) will be further explained with specific examples as follows. CH3=C(CH3)-COOCH2CH2OHCH2
=C(CH3)-COOCH2CH2CH2OHCH2
=C(CH3)-COOCH2CH(CH3)OHCH
2=C(CH3)-COOCH2CH2CH2CH2O
HCH2=C(CH3)-COOCH2CH2OCH2
CH2OH CH2=CH-COOCH2CH(CH3)OHCH2
=CH-COOCH2CH2CH2CH2OHCH2=
CH-CH2OH CH2=CH-CH2CH2OCH2CH2OHCH2
=C(CH3)-CONHCH2CH2OHCH2=C
H-CONHCH2CH2OHCH2=C(CH3)-
COOH CH2=CH-COOH CH2=C(CH3)-CONHCH2COOHCH2
=CH-CH2-COOH

【0030】[0030]

【化11】[Chemical formula 11]

【0031】第1工程および第2工程に示した交換反応
は触媒の存在下または非存在下に行なわれる。触媒とし
ては無機酸(塩酸,硝酸,硫酸,燐酸等),有機酸(蟻
酸,酢酸,プロピオン酸,しゅう酸,p−トルエンスル
ホン酸等),有機アミン化合物(トリエチルアミン,ト
リプロピルアミン等),有機アルカリ金属化合物(ナト
リウムメトキシド,ナトリウムエトキシド,カリウムメ
トキシド,カリウムエトキシド,カリウム−t−ブトキ
シド等),ゼオライト類,酸性もしくは塩基性イオン交
換樹脂,金属酸化物(Ga2O3 ,Tl2O3 ,S
b2O3,Al2O3等)等の液体状あるいは固体状の
酸または塩基を挙げることができる。中でも特に好まし
いのは、反応後の除去が容易という点で固体状触媒を用
いることが推奨される。
The exchange reactions shown in the first and second steps are carried out in the presence or absence of a catalyst. Catalysts include inorganic acids (hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, etc.), organic acids (formic acid, acetic acid, propionic acid, oxalic acid, p-toluenesulfonic acid, etc.), organic amine compounds (triethylamine, tripropylamine, etc.), and organic acids. Alkali metal compounds (sodium methoxide, sodium ethoxide, potassium methoxide, potassium ethoxide, potassium t-butoxide, etc.), zeolites, acidic or basic ion exchange resins, metal oxides (Ga2O3, Tl2O3, S
Examples include liquid or solid acids or bases such as b2O3, Al2O3, etc.). Among these, it is particularly preferred to use a solid catalyst because it can be easily removed after the reaction.

【0032】また上記交換反応は、溶媒中または無溶媒
下に0〜200 ℃、好ましくは40〜130 ℃に加
温され、また反応系は加圧下、常圧下、減圧下の如何を
問わず、また更に(化9)に示した反応式に従って副生
するアルコール類またはカルボン酸類を除去しつつ反応
を行うことも可能である。反応系に用いる溶媒としては
、反応の進行に悪影響を与えない限り全て使用でき、代
表的なものとしては、トルエン,キシレン等の芳香族炭
化水素系溶媒;ヘキサン,ヘプタン,オクタン等の脂肪
族炭化水素系溶媒;クロロホルム,塩化メチレン,ジク
ロロエタン等のハロゲン化炭化水素系溶媒;テトラヒド
ロフラン,ジオキサン,n−ブチルエーテル等のエーテ
ル系溶媒;メチルエチルケトン,メチルイソブチルケト
ン等のケトン系溶媒が使用される。
[0032] The above exchange reaction is carried out in a solvent or in the absence of a solvent at a temperature of 0 to 200°C, preferably 40 to 130°C, and the reaction system may be under pressure, normal pressure, or reduced pressure. Furthermore, it is also possible to carry out the reaction while removing by-product alcohols or carboxylic acids according to the reaction formula shown in (Chemical Formula 9). Any solvent can be used in the reaction system as long as it does not adversely affect the progress of the reaction. Typical examples include aromatic hydrocarbon solvents such as toluene and xylene; aliphatic carbonized solvents such as hexane, heptane, and octane. Hydrogen solvents; halogenated hydrocarbon solvents such as chloroform, methylene chloride and dichloroethane; ether solvents such as tetrahydrofuran, dioxane and n-butyl ether; ketone solvents such as methyl ethyl ketone and methyl isobutyl ketone are used.

【0033】[0033]

【発明の効果】本発明は上記の様に構成されているので
、アルコキシ基またはアシルオキシ基を有する有機珪素
化合物を、アルコール類またはカルボン酸類と交換反応
を行うに際して、モノ交換体化合物を高収率に製造する
ことが可能となった。
Effects of the Invention Since the present invention is constructed as described above, when an organosilicon compound having an alkoxy group or an acyloxy group is exchanged with an alcohol or a carboxylic acid, a monoexchanger compound can be produced in high yield. It became possible to manufacture

【0034】[0034]

【実施例】次に本発明を実施例により更に具体的に説明
するが、本発明はこれら実施例に限定されるものではな
い。
EXAMPLES Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to these Examples.

【0035】実施例1 (1) 多交換体副生物の調製 テトラメトキシシラン400gと2−ヒドロキシエチル
メタクリレート171gと、アンバーリスト15(酸性
イオン交換樹脂,ローム・アンド・ハース・ジャパン製
)3g を200mmHg 下に80℃まで2時間かけ
て昇温し、留出する液(メタノール)がなくなるまで同
温度で保持した。室温まで冷却し、アンバーリスト15
を濾別し、その濾液から10mmHgの減圧下に過剰の
テトラメトキシシランを留去し第1工程を終了した。残
渣にフェノチアジン(重合禁止剤)60mgを添加し、
0.2mmHg の減圧下に蒸留底部液の温度が130
 ℃になるまでまで蒸留を行い、メタクリロキシエトキ
シトリメトキシシラン(モノ交換体)192gを得た。 このときの蒸留残渣すなわち多交換体副生物100gの
組成をHPLCにより分析すると、メタクリロキシエト
キシトリメトキシシラン13.5g(0.0539モル
),ジ(メタクリロキシエトキシ)ジメトキシシラン6
8.5g(0.197 モル),トリ(メタクリロキシ
エトキシ)メトキシシラン13.5g(0.0302モ
ル))を含んでいた。
Example 1 (1) Preparation of multi-exchanger by-product 400 g of tetramethoxysilane, 171 g of 2-hydroxyethyl methacrylate, and 3 g of Amberlyst 15 (acidic ion exchange resin, manufactured by Rohm & Haas Japan) were heated to 200 mmHg. The temperature was raised to 80° C. over 2 hours, and maintained at the same temperature until no liquid (methanol) was distilled out. Cool to room temperature and add Amberlyst 15
was separated by filtration, and excess tetramethoxysilane was distilled off from the filtrate under reduced pressure of 10 mmHg to complete the first step. Add 60 mg of phenothiazine (polymerization inhibitor) to the residue,
The temperature of the distillation bottom liquid was 130°C under a reduced pressure of 0.2mmHg.
Distillation was carried out until the temperature reached ℃, and 192 g of methacryloxyethoxytrimethoxysilane (monoexchanger) was obtained. HPLC analysis of the composition of the distillation residue, 100 g of the multi-exchanger by-product, revealed that 13.5 g (0.0539 mol) of methacryloxyethoxytrimethoxysilane, 6 g of di(methacryloxyethoxy)dimethoxysilane,
8.5 g (0.197 mol), tri(methacryloxyethoxy)methoxysilane 13.5 g (0.0302 mol)).

【0036】(2) 第1工程 上で得た多交換体副生物100g,テトラメトキシシラ
ン357.6g(2.35 モル)および2−ヒドロキ
シエチルメタクリレート100.5g(0.772モル
)にアンバーリスト15を3g 加え200mmHg 
の下で80℃まで2時間かけて昇温し、留出する液(メ
タノール)がなくなるまで同温度で保持した。室温まで
冷却し、アンバーリスト15を濾別し、その濾液を10
mmHgの減圧下に加熱して過剰のテトラメトキシシラ
ンを留去し、残渣301gを得た。
(2) Amberlyst was added to 100 g of the polyexchanger by-product obtained in the first step, 357.6 g (2.35 mol) of tetramethoxysilane, and 100.5 g (0.772 mol) of 2-hydroxyethyl methacrylate. Add 3g of 15 and make 200mmHg
The temperature was raised to 80° C. over 2 hours under the following conditions, and the temperature was maintained until no liquid (methanol) was distilled out. Cool to room temperature, filter off Amberlyst 15, and remove the filtrate from 10
Excess tetramethoxysilane was distilled off by heating under reduced pressure of mmHg to obtain 301 g of a residue.

【0037】(3) 第2工程 上で得た残渣にフェノチアジン60mgを加え、0.2
mmHg の減圧下に蒸留低部液温度が130 ℃にな
るまで蒸留を行い、メタクリロキシエトキシトリメトキ
シシラン191g(0.763モル)を得た。これは、
(2) において使用した2−ヒドロキシエチルメタク
リレートに対して98%の収率であることを示している
(3) Add 60 mg of phenothiazine to the residue obtained in the second step, and add 0.2
Distillation was carried out under a reduced pressure of mmHg until the temperature of the lower part of the distillation reached 130° C. to obtain 191 g (0.763 mol) of methacryloxyethoxytrimethoxysilane. this is,
This shows a yield of 98% based on the 2-hydroxyethyl methacrylate used in (2).

【0038】実施例2〜7 実施例1のテトラメトキシシランのかわりに表1のXを
用い、2−ヒドロキシエチルメタクリレートのかわりに
表1のYを用いて、実施例1と同様に反応を行なった。 尚実施例5においては、触媒をTl2O3に替えて行な
った。また実施例3,7においては交換反応実施時の圧
力を200mmHg から130mmHg に変更した
。結果を表1に示す。
Examples 2 to 7 Reactions were carried out in the same manner as in Example 1, using X in Table 1 instead of tetramethoxysilane in Example 1, and Y in Table 1 in place of 2-hydroxyethyl methacrylate. Ta. In Example 5, the catalyst was changed to Tl2O3. In Examples 3 and 7, the pressure during exchange reaction was changed from 200 mmHg to 130 mmHg. The results are shown in Table 1.

【0039】[0039]

【表1】[Table 1]

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  一般式 【化1】 (式中R1は炭素数10以下の炭化水素残基、R2は水
素原子または炭素数5以下のアルキル基または炭素数5
以下のアシル基、nは0,1または2をそれぞれ意味す
る)で示される化合物(A)、および一般式:R3−O
H                        
        (B)(式中R3は炭素数20以下の
有機残基を意味する)で示される化合物(B)から、一
般式 【化2】 (式中R1,R2,R3およびnはそれぞれ前と同じ意
味)で示されるモノ交換体化合物(C)を製造する方法
において、前記化合物(A)と前記化合物(B)との反
応によって生成する生成物のうち、前記モノ交換体化合
物(C)を、一般式 【化3】 で示されるジ交換体化合物(D)や、一般式【化4】 で示されるトリ交換体化合物(E)等の多交換体副生物
から分離採取すると共に、分離除去された前記多交換体
副生物を化合物(A)と化合物(B)との反応系に混合
して交換反応を行なわせることを特徴とするモノ交換体
化合物の製造方法。
Claim 1: General formula [Formula 1] (wherein R1 is a hydrocarbon residue having 10 or less carbon atoms, R2 is a hydrogen atom, an alkyl group having 5 or less carbon atoms, or a carbon number 5 or less)
Compound (A) represented by the following acyl group, n means 0, 1 or 2, respectively), and the general formula: R3-O
H
(B) (In the formula, R3 means an organic residue having 20 or less carbon atoms) From the compound (B) represented by the general formula [Chemical formula 2] (wherein R1, R2, R3 and n are the same as before, In the method for producing a monoexchanger compound (C) represented by (meaning), among the products produced by the reaction of the compound (A) and the compound (B), the monoexchanger compound (C) is The di-exchanger compound (D) represented by the general formula [Chemical formula 3] and the tri-exchanger compound (E) represented by the general formula [Chemical formula 4] are separated and collected from the multi-exchanger by-products, and are also separated and removed. A method for producing a mono-exchanger compound, characterized in that the multi-exchanger by-product is mixed into a reaction system of compound (A) and compound (B) to carry out an exchange reaction.
JP10196291A 1991-04-05 1991-04-05 Production of mono-exchanger compound in organosilicone compound Withdrawn JPH04308595A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10196291A JPH04308595A (en) 1991-04-05 1991-04-05 Production of mono-exchanger compound in organosilicone compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10196291A JPH04308595A (en) 1991-04-05 1991-04-05 Production of mono-exchanger compound in organosilicone compound

Publications (1)

Publication Number Publication Date
JPH04308595A true JPH04308595A (en) 1992-10-30

Family

ID=14314495

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10196291A Withdrawn JPH04308595A (en) 1991-04-05 1991-04-05 Production of mono-exchanger compound in organosilicone compound

Country Status (1)

Country Link
JP (1) JPH04308595A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06228165A (en) * 1993-01-29 1994-08-16 Shin Etsu Chem Co Ltd Organosilicon compound and its production

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06228165A (en) * 1993-01-29 1994-08-16 Shin Etsu Chem Co Ltd Organosilicon compound and its production

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