Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP2931015B2 - Polymerization catalyst composition - Google Patents
[go: Go Back, main page]

JP2931015B2 - Polymerization catalyst composition - Google Patents

Polymerization catalyst composition

Info

Publication number
JP2931015B2
JP2931015B2 JP3247290A JP3247290A JP2931015B2 JP 2931015 B2 JP2931015 B2 JP 2931015B2 JP 3247290 A JP3247290 A JP 3247290A JP 3247290 A JP3247290 A JP 3247290A JP 2931015 B2 JP2931015 B2 JP 2931015B2
Authority
JP
Japan
Prior art keywords
peroxide
polymerization
catalyst composition
polymerization catalyst
present
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 - Fee Related
Application number
JP3247290A
Other languages
Japanese (ja)
Other versions
JPH03237108A (en
Inventor
一男 津布子
信一 倉本
和彦 梅村
ひでみ 植松
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.)
Ricoh Co Ltd
Original Assignee
Ricoh 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 Ricoh Co Ltd filed Critical Ricoh Co Ltd
Priority to JP3247290A priority Critical patent/JP2931015B2/en
Publication of JPH03237108A publication Critical patent/JPH03237108A/en
Application granted granted Critical
Publication of JP2931015B2 publication Critical patent/JP2931015B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Polymerization Catalysts (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は有機過酸化物を含む重合触媒組成物に関す
る。
Description: TECHNICAL FIELD The present invention relates to a polymerization catalyst composition containing an organic peroxide.

[従来の技術] 有機過酸化物は分子中−O−O−結合を持ち、比較的
低い温度で熱分解し、容易に遊離ラジカルを発生するの
で、ラジカル重合におけるラジカル源、即ち重合開始剤
として使用されていることは周知である。一般にこの化
合物は常温で安定であり、オレフィンやビニル系モノマ
ーの重合及び共重合の他、不飽和ポリエステルの硬化に
も利用されているが、火花、加熱、摩擦、衝撃、不純物
(酸又はアルカリ)の混入等により分解又は爆発すると
いう欠点があり、しかもこの爆発に対する感度はピクリ
ン酸、TNT火薬等よりはるかに鋭敏である。このように
有機過酸化物は取扱が危険なため、特公昭48−16715、
特開昭54−160487にみられるように製造工程ではジオク
チルフタレート、ジブチルフタレート等で希釈し、又保
存中は硫酸カルシウム、炭酸カルシウム、第2リン酸カ
ルシウム、水、脂肪族炭化水素等の純品で希釈して使用
されている。しかしこうして得られる重合触媒組成物に
おいては経時と共に過酸化物が次第に分解するし、良好
な重合効率が得られないばかりでなく、希釈剤が重合製
品に残存するため、高純度の製品を得る場合は更に重合
製品の精製又は乾燥を必要としていた。
[Prior Art] Organic peroxides have an -O-O- bond in the molecule, thermally decompose at a relatively low temperature, and easily generate free radicals. Therefore, as a radical source in radical polymerization, that is, as a polymerization initiator, It is well known that it is used. Generally, this compound is stable at normal temperature and is used for curing unsaturated polyesters in addition to polymerization and copolymerization of olefins and vinyl monomers. However, sparks, heating, friction, impact, impurities (acid or alkali) Has the disadvantage that it decomposes or explodes due to the incorporation of it, and is much more sensitive to this explosion than picric acid, TNT or the like. Because organic peroxides are dangerous to handle, Japanese Patent Publication No. 48-16715,
As shown in JP-A-54-160487, in the manufacturing process, dilute with dioctyl phthalate, dibutyl phthalate, etc., and during storage, dilute with pure products such as calcium sulfate, calcium carbonate, dibasic calcium phosphate, water and aliphatic hydrocarbons Has been used. However, in the polymerization catalyst composition thus obtained, peroxides gradually decompose over time, and not only good polymerization efficiency is not obtained, but also a diluent remains in the polymerization product, so that a high-purity product is obtained. Required further purification or drying of the polymerized product.

[発明が解決しようとする課題] 本発明の目的は保存安定性及び重合効率、撥水性を向
上すると共に重合製品の精製や乾燥を必要としない重合
触媒組成物を提供することである。
[Problems to be Solved by the Invention] An object of the present invention is to provide a polymerization catalyst composition which improves storage stability, polymerization efficiency and water repellency and does not require purification or drying of a polymer product.

[課題を解決するための手段] 本発明者らは、前記した課題を解決するため鋭意検討
した結果、有機過酸化物にフッ素系オイルを混合するこ
とが有効であることを知見し、本発明に至った。
Means for Solving the Problems The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, have found that it is effective to mix a fluorine-based oil with an organic peroxide. Reached.

すなわち、本発明の構成は有機過酸化物と保存安定化
剤としてのパーフルオロ系オイルとを主成分とする保存
安定化されたラジカル重合用触媒組成物である。
That is, the constitution of the present invention is a storage-stabilized radical polymerization catalyst composition containing an organic peroxide and a perfluoro-based oil as a storage stabilizer as main components.

本発明に使用するフッ素系オイルは炭化水素系オイル
の水素をフッ素で置換したものである。これらのうちパ
ーフルオロ系オイルがより好ましい。以下にパーフルオ
ロ系オイルの例とそれらの物性を表にして示す。
The fluorinated oil used in the present invention is obtained by replacing hydrogen of a hydrocarbon oil with fluorine. Of these, perfluoro-based oils are more preferred. Hereinafter, examples of perfluoro-based oils and their physical properties are shown in a table.

フッ素系オイルは高沸点、高引火点を有する無臭の不
活性液体で酸、アルカリ等の不純物を全く含まない。従
ってこれらのフッ素系オイルによって過酸化物が分解し
たり、爆発する恐れはない。又このため過酸化物の保存
安定性を著しく向上することができる。又各種重合法、
例えば塊状重合のような発熱反応においても過酸化物と
良く混和し、且つラジカルの分解速度を適正に制御する
ため、高重合効率で重合体を製造することができる。更
にこの脂肪族炭化水素は重合製品中に残存しないので、
精製又は乾燥を省略することができる等の利点を有して
いる。
The fluorinated oil is an odorless inert liquid having a high boiling point and a high flash point and contains no impurities such as acids and alkalis. Therefore, there is no danger of peroxide being decomposed or exploding by these fluorinated oils. Therefore, the storage stability of the peroxide can be remarkably improved. Also various polymerization methods,
For example, even in an exothermic reaction such as bulk polymerization, a polymer can be produced with high polymerization efficiency because it is well mixed with peroxide and appropriately controls the decomposition rate of radicals. Furthermore, since this aliphatic hydrocarbon does not remain in the polymerized product,
It has the advantage that purification or drying can be omitted.

一方、有機過酸化物としては従来使用されているもの
が全て使用でき、例えばメチルエチルケトンパーオキサ
イド、シクロヘキサンパーオキサイド等のケトンパーオ
キサイトド;1,1−ビス(t−ブチルパーオキシ)シクロ
ヘキサン、n−ブチル−4,4−ビス(t−ブチルパーオ
キシ)パリレート等のパーオキシケタール;ジアルキル
パーオキサイド;ベンゾイルパーオキサイド、コハク酸
パーオキサイド、デカノイルパーオキサイド、2,4−ジ
クロロベンゾイルパーオキサイド等のジアシルパーオキ
サイド;2,5−ジメチル−2,5−ジ(ベンゾイルパーオキ
サイド)ヘキサン、t−ブチルパーオキシマレイン酸、
t−ブチルパーオキシイソプロピルカーボネート、ジ−
t−ブチルジパーオキシフタレート等のパーオキシエス
テル等が挙げられる。
On the other hand, as the organic peroxide, all conventionally used organic peroxides can be used. For example, ketone peroxides such as methyl ethyl ketone peroxide and cyclohexane peroxide; 1,1-bis (t-butylperoxy) cyclohexane, n Peroxyketals such as -butyl-4,4-bis (t-butylperoxy) parylate; dialkyl peroxides; benzoyl peroxide, succinic peroxide, decanoyl peroxide, and 2,4-dichlorobenzoyl peroxide; Diacyl peroxide; 2,5-dimethyl-2,5-di (benzoyl peroxide) hexane, t-butylperoxymaleic acid,
t-butyl peroxyisopropyl carbonate, di-
Peroxyesters such as t-butyl diperoxyphthalate and the like can be mentioned.

本発明の組成物においては前述のような目的から有機
過酸化物/フッ素系オイルの重量比は一般に30〜90/70
〜10、好ましくは50〜75/50〜25程度が適当である。又
本発明の組成物は乳化重合、塊状重合、溶液重合等の重
合反応に適用できる。この場合、通常モノマーに対し0.
05〜2.0wt%使用される。
In the composition of the present invention, the weight ratio of the organic peroxide / fluorinated oil is generally 30 to 90/70 for the above-mentioned purpose.
-10, preferably about 50-75 / 50-25. Further, the composition of the present invention can be applied to polymerization reactions such as emulsion polymerization, bulk polymerization and solution polymerization. In this case, usually 0.
Used from 05 to 2.0 wt%.

なお本発明の組成物には他の溶剤、例えばトルエン、
キシレン、高級アルコール、脂肪族炭化水素等を全量に
対し約20重量%以下加えることができる。
Note that the composition of the present invention contains other solvents, for example, toluene,
Xylene, higher alcohols, aliphatic hydrocarbons and the like can be added in an amount of about 20% by weight or less based on the total amount.

以下に実施例を示す。 Examples will be described below.

実施例1 2,4−ジクロロベンゾイルクロライド500g及びパーフ
ルオロシクロヘキサン200gを4つ口フラスコに取り混合
する。次いでモノエタノールアミン4gを加え80℃で2時
間反応させた後、過酸化水素100gを5時間に亘って滴下
し、更に80℃で10時間反応させ、2,4−ジクロロベンゾ
イルクロライドを過酸化水素で酸化した。これを分液ロ
ート中で水洗後、水を分解して、2,4−ジクロロベンゾ
イルパーオキサイド及びパーフルオロシクロヘキサンよ
りなる重合触媒組成物(過酸化物濃度70.60%)を得
た。
Example 1 500 g of 2,4-dichlorobenzoyl chloride and 200 g of perfluorocyclohexane were placed in a four-necked flask and mixed. Then, after adding 4 g of monoethanolamine and reacting at 80 ° C. for 2 hours, 100 g of hydrogen peroxide was added dropwise over 5 hours, and further reacted at 80 ° C. for 10 hours to convert 2,4-dichlorobenzoyl chloride to hydrogen peroxide. Oxidation. This was washed with water in a separating funnel, and then water was decomposed to obtain a polymerization catalyst composition (peroxide concentration: 70.60%) comprising 2,4-dichlorobenzoyl peroxide and perfluorocyclohexane.

又比較例1として本実施例でパーフルオロシクロヘキ
サンを除いて合成し、且つ水洗後減圧乾燥した他は同じ
方法で重合触媒組成物を得た。
Further, as Comparative Example 1, a polymerization catalyst composition was obtained in the same manner as in Example 1 except that perfluorocyclohexane was omitted, and washing was performed with water, followed by drying under reduced pressure.

次にこれら組成物について調整直後及び6カ月間常温
保存後の過酸化物含有量及び活性酸素量を測定した結果
を表−1に示す。
Next, the results of measuring the peroxide content and the active oxygen content of these compositions immediately after preparation and after storage at room temperature for 6 months are shown in Table 1.

表−1から判るように本発明品は比較品に比べて過酸
化物含有量及び活性酸素量の経時変化が少なく、従って
保存安定性に優れている。なお本発明品は爆発の恐れは
全く認められなかった。
As can be seen from Table 1, the product of the present invention has less change over time in the peroxide content and the amount of active oxygen than the comparative product, and thus has excellent storage stability. The product of the present invention did not show any risk of explosion.

実施例2 塩化ベンゾイル500g及びパーフルオロブチルテトラヒ
ドロフラン200gを4つ口フラスコに取り混合する。これ
にピリジン1gを加え、85℃で4時間反応させた後、過酸
化水素200gを8時間に亘って滴下し、更に5時間反応さ
せ、塩化ベンゾイルを過酸化水素で酸化した。これを分
液ロート中で水洗後、水を分離して過酸化ベンゾイル及
びパーフルオロブチルテトラヒドロフランよりなる重合
触媒組成物(過酸化物濃度82%)を得た。
Example 2 500 g of benzoyl chloride and 200 g of perfluorobutyltetrahydrofuran are placed in a four-necked flask and mixed. 1 g of pyridine was added thereto, and the mixture was reacted at 85 ° C. for 4 hours. Then, 200 g of hydrogen peroxide was added dropwise over 8 hours, and the mixture was further reacted for 5 hours to oxidize benzoyl chloride with hydrogen peroxide. This was washed with water in a separatory funnel, and water was separated to obtain a polymerization catalyst composition comprising benzoyl peroxide and perfluorobutyltetrahydrofuran (peroxide concentration: 82%).

一方、比較例2として98%純度の過酸化ベンゾイルを
用意した。
On the other hand, as Comparative Example 2, benzoyl peroxide having a purity of 98% was prepared.

次にこれらの組成物について爆発性をテストした。ま
ず本発明品500gを入れたビーカー(5容量)及び比較
品850gを入れたビーカー(5容量)を夫々8個用意
し、各ビーカーに700℃に加熱した遠赤外ヒーターを近
付けると、比較品はいずれも同時に爆発したのに対し、
本発明品はいずれも爆発しなかった。
The compositions were then tested for explosiveness. First, eight beakers (5 volumes) each containing 500 g of the product of the present invention and 850 g of comparative products were prepared, and a far-infrared heater heated to 700 ° C. was brought close to each beaker. Exploded at the same time,
None of the products of the present invention exploded.

実施例3〜8 実施例1において過酸化物及びフッ素系オイル又は希
釈剤として夫々表−2記載のものを使用し、同様に示す
過酸化物濃度の重合触媒組成物を得た。これらの活性酸
素量を表−8に示した。
Examples 3 to 8 In Example 1, the peroxide and the fluorinated oil or those shown in Table 2 were used as diluents, respectively, to obtain polymerization catalyst compositions having the same peroxide concentrations as shown in Table 2. These active oxygen contents are shown in Table-8.

表−3から判るように、実施例3〜8の組成物も保存
安定性が優れている。
As can be seen from Table 3, the compositions of Examples 3 to 8 also have excellent storage stability.

更に以上のようにして得られた各重合触媒組成物を用
いて重合反応を行った。まず攪拌機、温度計、冷却装置
を備えた3つ口フラスコ(2容量)にイソオクタン30
0gを取り、90℃に加熱した。次にメチルメタアクリレー
ト150g、メタクリル酸20g、及び過酸化物8gを汲む各組
成物を混合し、前記フラスコ中に1時間に亘って滴下重
合させた。重合結果を表−4に示す。
Further, a polymerization reaction was carried out using each polymerization catalyst composition obtained as described above. First, isooctane 30 was placed in a three-necked flask (2 volumes) equipped with a stirrer, thermometer, and cooling device.
Take 0 g and heat to 90 ° C. Next, each composition containing 150 g of methyl methacrylate, 20 g of methacrylic acid, and 8 g of peroxide was mixed and polymerized dropwise in the flask over 1 hour. Table 4 shows the polymerization results.

[発明の効果] 以上説明したように、本発明重合触媒組成物は、保存
安定性に優れ、かつ、重合効率、及びこれにより得られ
た重合体の撥水性を向上することができる。
[Effects of the Invention] As described above, the polymerization catalyst composition of the present invention is excellent in storage stability, and can improve polymerization efficiency and water repellency of a polymer obtained thereby.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 植松 ひでみ 東京都大田区中馬込1丁目3番6号 株 式会社リコー内 (56)参考文献 特開 昭46−5243(JP,A) 特開 昭46−7287(JP,A) 特開 昭48−96678(JP,A) 特開 昭49−14407(JP,A) 特開 昭49−74291(JP,A) 特開 昭49−90787(JP,A) 特開 昭49−118789(JP,A) 特開 昭49−125490(JP,A) 特開 昭51−41086(JP,A) 特開 昭51−132294(JP,A) 特開 昭52−887(JP,A) 特開 昭55−139357(JP,A) 特開 昭58−139210(JP,A) 特開 昭61−152652(JP,A) 特開 昭61−152653(JP,A) 特開 昭61−291676(JP,A) (58)調査した分野(Int.Cl.6,DB名) C08F 4/00 - 4/82 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Hidemi Uematsu 1-3-6 Nakamagome, Ota-ku, Tokyo Inside Ricoh Company, Ltd. (56) References JP-A-46-5243 (JP, A) JP-A Sho 46-7287 (JP, A) JP-A-48-96678 (JP, A) JP-A-49-14407 (JP, A) JP-A-49-74291 (JP, A) JP-A-49-90787 (JP, A) A) JP-A-49-118789 (JP, A) JP-A-49-125490 (JP, A) JP-A-51-41086 (JP, A) JP-A-51-132294 (JP, A) JP-A Sho 52 JP-A-8-887 (JP, A) JP-A-55-139357 (JP, A) JP-A-58-139210 (JP, A) JP-A-61-152652 (JP, A) JP-A-61-152653 (JP, A) JP-A-61-291676 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C08F 4/00-4/82

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】有機過酸化物と保存安定化剤としてのパー
フルオロ系オイルとを主成分とする保存安定化されたラ
ジカル重合用触媒組成物。
1. A storage-stabilized radical polymerization catalyst composition comprising an organic peroxide and a perfluoro-based oil as a storage stabilizer as main components.
JP3247290A 1990-02-15 1990-02-15 Polymerization catalyst composition Expired - Fee Related JP2931015B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3247290A JP2931015B2 (en) 1990-02-15 1990-02-15 Polymerization catalyst composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3247290A JP2931015B2 (en) 1990-02-15 1990-02-15 Polymerization catalyst composition

Publications (2)

Publication Number Publication Date
JPH03237108A JPH03237108A (en) 1991-10-23
JP2931015B2 true JP2931015B2 (en) 1999-08-09

Family

ID=12359919

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3247290A Expired - Fee Related JP2931015B2 (en) 1990-02-15 1990-02-15 Polymerization catalyst composition

Country Status (1)

Country Link
JP (1) JP2931015B2 (en)

Also Published As

Publication number Publication date
JPH03237108A (en) 1991-10-23

Similar Documents

Publication Publication Date Title
EP0186215B1 (en) Fluorine-containing diacylperoxides and use thereof
US3493530A (en) Process for the polymerization and copolymerization of halogenated olefins
US2423497A (en) Production of products having recurring arylethylene units with termini from a saturated halogenated alkane
US2433015A (en) Reaction of ethylene with organic carboxylic acids
JP2931015B2 (en) Polymerization catalyst composition
JPH035434A (en) Production of telomer alcohol
JPS6160082B2 (en)
US3631115A (en) Telomerization process for the preparation of halogenated hydrocarbons
GB2148286A (en) Preparation of chlorotrifluoroethylene telomers with fluoroxytrifluromethane and bisfluoroxydifluoro methane
JP2881213B2 (en) Polymerization catalyst composition
US2507568A (en) Telomers of monoolefins and saturated halogenated carboxylic acids, esters, and anhydrides
US2396261A (en) Products
JPH06107650A (en) Method for producing hexafluoropropene oxide
JP7647235B2 (en) Peroxyester composition and polymerization initiator
DE2632294A1 (en) Oligomeric silyl ether cpds. - used as free radical polymerisation initiators, giving rapid cure at relatively low temp.
US2757167A (en) Preparation of fluorinated polymers with oxygen difluoride catalyst
CA1104159A (en) Chlorination of meta-phenoxytoluene
US3342872A (en) 2, 2-bis-(4, 4-ditertiary-butyl-peroxycyclohexyl)-propane
US3429934A (en) Telomerization process for the preparation of halogenated hydrocarbons
Asscher et al. Telomerization of ethylene and carbon tetrachloride. Novel initiating system
US3342778A (en) Perfluoroalkyl perfluorovinyl ketones and their polymers
JPS5837286B2 (en) Method for producing low molecular weight tertiary alcohol
JPH0556765B2 (en)
US3142537A (en) Novel compounds containing sulphur, fluorine, and oxygen
US2830097A (en) Fluorination of a telomer of trichlorobromomethane and vinylidene chloride

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees