JPH0362840A - Vinyl chloride resin for laminated glass - Google Patents

Vinyl chloride resin for laminated glass

Info

Publication number
JPH0362840A
JPH0362840A JP11647789A JP11647789A JPH0362840A JP H0362840 A JPH0362840 A JP H0362840A JP 11647789 A JP11647789 A JP 11647789A JP 11647789 A JP11647789 A JP 11647789A JP H0362840 A JPH0362840 A JP H0362840A
Authority
JP
Japan
Prior art keywords
vinyl chloride
laminated glass
polymerization
glass
chloride resin
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
JP11647789A
Other languages
Japanese (ja)
Other versions
JP2779832B2 (en
Inventor
Toshihiko Hori
登志彦 堀
Eitaro Nakamura
栄太郎 中村
Toyoichi Arai
新井 豊一
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.)
Zeon Corp
Original Assignee
Nippon Zeon 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 Zeon Co Ltd filed Critical Nippon Zeon Co Ltd
Priority to JP11647789A priority Critical patent/JP2779832B2/en
Priority to EP19900304929 priority patent/EP0397439B1/en
Priority to DE69017748T priority patent/DE69017748T2/en
Priority to US07/520,426 priority patent/US5091487A/en
Publication of JPH0362840A publication Critical patent/JPH0362840A/en
Application granted granted Critical
Publication of JP2779832B2 publication Critical patent/JP2779832B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Laminated Bodies (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Polymerisation Methods In General (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は優れた接着強度を有する塩化ビニル樹脂に関し
、さらに詳細には耐貫通性、耐衝撃性に優れた合せガラ
スを提供する合せガラス用塩化ビニル樹脂に関する。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to a vinyl chloride resin having excellent adhesive strength, and more particularly to a polyvinyl chloride resin for use in laminated glass that provides laminated glass with excellent penetration resistance and impact resistance. Regarding vinyl chloride resin.

(従来の技術) 従来から、安全合せガラス用中間膜として可塑化ポリビ
ニルブチラール膜を使用することが知られている。しか
し、この可塑化ポリビニルブチラール膜は膜表面の粘着
性が強いため、製膜後の捲回時に膜同志が自着するとい
う問題を有し、かかる粘着を防ぐ目的で表面にエンボス
加工を施し更に重炭酸ソーダ等の粘着防止剤を散布して
いる。
(Prior Art) It has been known to use a plasticized polyvinyl butyral film as an interlayer film for safety laminated glass. However, this plasticized polyvinyl butyral film has a strong adhesion on the film surface, so there is a problem that the films adhere to each other during winding after film formation.In order to prevent such adhesion, the surface is embossed and further An anti-blocking agent such as bicarbonate of soda is sprayed.

一方、この様な膜同志の自若の少ない膜として、可塑剤
を約40重量%含有する塩化ビニル−グリシジルメタク
リレート共重合体膜を使用することは公知である。又、
公開特許公報昭55−162451にエステル及びビニ
ルエーテルより選ばれる少なくとも1種のモノマーとを
共重合して得られる共重合体に可塑剤が加えられてなる
中間膜を使用することが提案されている。これらの塩化
ビニル系共重合体のグリシジルメタクリレート含有量を
変化させ、ガラスへの接着強度を改善することができる
が、グリシジルメタクリレート含有量を増加させると合
せガラスの耐貫通強度が低下してしまい、接着強度と耐
貫通強度を両立させることは難しい。
On the other hand, it is known that a vinyl chloride-glycidyl methacrylate copolymer film containing about 40% by weight of a plasticizer is used as such a film with little self-reflection. or,
The use of an interlayer film made by adding a plasticizer to a copolymer obtained by copolymerizing at least one monomer selected from esters and vinyl ethers is proposed in Japanese Patent Publication No. 55-162451. The adhesion strength to glass can be improved by changing the glycidyl methacrylate content of these vinyl chloride copolymers, but increasing the glycidyl methacrylate content reduces the penetration resistance strength of the laminated glass. It is difficult to achieve both adhesive strength and penetration resistance.

また、重合時の収率が低下したり、熱安定性が不足し、
着色の原因ともなる。
In addition, the yield during polymerization may decrease, thermal stability may be insufficient,
It can also cause discoloration.

(発明が解決しようとする課題) 本発明の目的は接着強度、耐貫通性の優れた合せガラス
用塩化ビニル樹脂を提供することにある。
(Problems to be Solved by the Invention) An object of the present invention is to provide a vinyl chloride resin for laminated glass that has excellent adhesive strength and penetration resistance.

かくして本発明によれば、 (1)粒径が5μ以下で粒子の外殻部のエポキシ基含有
量が粒子の中核部のエポキシ基含有量より高いことを特
徴とする粒子、及びその集合体からなる合せガラス用塩
化ビニル樹脂、 (2)塩化ビニルとエポキシ基を有する単量体と任意成
分であるこれらと共重合可能な単量体との共重合体から
なることを特徴とする(1)に記載の合せガラス用塩化
ビニル樹脂 が提供される。
Thus, according to the present invention, (1) particles having a particle size of 5μ or less and having a higher epoxy group content in the outer shell than the epoxy group content in the core of the particle, and aggregates thereof; A vinyl chloride resin for laminated glass, (2) consisting of a copolymer of vinyl chloride, a monomer having an epoxy group, and an optional monomer copolymerizable with these (1) Provided is a vinyl chloride resin for laminated glass as described in .

(課題を解決するための手段) 本発明において用いられるエポキシ基を有する単量体の
例としては、アリルグリシジルエーテル、メタリルグリ
シジルエーテル等の不飽和アルコールのグリシジルエー
テル類、グリシジルメタクリレート、グリシジルアクリ
レート、グリシジルp−ビニルベンゾニー1−、メチル
グリシジルイタコネート、グリシジルエチルマレート、
グリシジルビニルスルホネート、グリシジル(メク)ア
リルスルホネ−1・等の不飽和酸のグリシジルエステル
類、ブタジエンモノオキザイド、ビニルシクロヘキセン
モノオキサイド、2−メチル−56−ニポキシヘキセン
等のエポキシドオレフィン類などがあげられる。
(Means for Solving the Problems) Examples of the monomer having an epoxy group used in the present invention include glycidyl ethers of unsaturated alcohols such as allyl glycidyl ether and methallyl glycidyl ether, glycidyl methacrylate, glycidyl acrylate, Glycidyl p-vinylbenzony 1-, methylglycidyl itaconate, glycidyl ethyl maleate,
Examples include glycidyl esters of unsaturated acids such as glycidyl vinyl sulfonate and glycidyl(mec)allylsulfone-1, and epoxide olefins such as butadiene monooxide, vinylcyclohexene monooxide, and 2-methyl-56-nipoxyhexene.

また、任意成分であるこれらと共重合可能な単量体の例
としては、酢酸ビニル、プロピオン酸ビニル等の脂肪酸
ビニル類、エヂレン、プロピレン等のオレフィン類、塩
化ビニリデン、弗化ビニリデン等のハロゲン化ビニリデ
ン類、イソブチルビニルエーテル、メチルビニルエーテ
ル、セチルビニルエーテル等のビニルエーテル類、塩化
アリル、メチルアリルエーテル等のアリル化合物類など
があげられる。
Examples of monomers that can be copolymerized with these optional components include fatty acid vinyls such as vinyl acetate and vinyl propionate, olefins such as ethylene and propylene, and halogenated monomers such as vinylidene chloride and vinylidene fluoride. Examples include vinylidenes, vinyl ethers such as isobutyl vinyl ether, methyl vinyl ether, and cetyl vinyl ether, and allyl compounds such as allyl chloride and methyl allyl ether.

これらの単量体を用いて、エポキシ基含有塩化ビニル樹
脂を得るには、塊状重合、懸濁重合、ミクロ懸濁重合、
乳化重合等の塩化ビニルの重合法として良く知られてい
る方法が採用可能である。
In order to obtain an epoxy group-containing vinyl chloride resin using these monomers, bulk polymerization, suspension polymerization, micro suspension polymerization,
Well-known methods for polymerizing vinyl chloride, such as emulsion polymerization, can be employed.

たとえば、カレンダーロール法、押出シートキャスティ
ング法、インフレーション法等の製膜加工法により合せ
がガラス中間膜を得る場合には、懸濁重合が好ましい。
For example, when obtaining a glass interlayer film by a film forming process such as a calender roll method, an extrusion sheet casting method, or an inflation method, suspension polymerization is preferred.

また、プラスチゾルとして使用する場合には、プラスチ
ゾルの流動性を適当に保つ目的からペースト加工用塩化
ビニル樹脂の重合法として賞用される乳化重合あるいは
ミクロ懸濁重合が好ましい。本発明の効果はいずれの重
合法においても発現するが、その効果は粒子径が5μ以
下と小さい乳化重合、ミクロ懸濁重合において大きく発
現する。粒子径が5μより大きいとエポキシ基が必ずし
も粒子の外層部に分布しなくなるのでガラスへの接着力
が不十分になる。
When used as a plastisol, emulsion polymerization or microsuspension polymerization, which is used as a polymerization method for vinyl chloride resin for paste processing, is preferred for the purpose of maintaining appropriate fluidity of the plastisol. Although the effects of the present invention are manifested in any polymerization method, the effects are most pronounced in emulsion polymerization and microsuspension polymerization in which the particle size is small, such as 5 μm or less. If the particle size is larger than 5 μm, the epoxy groups will not necessarily be distributed in the outer layer of the particles, resulting in insufficient adhesion to glass.

これらの重合方法を用いて、本発明の招脂を得るために
は、エポキシ基を有する単量体は、重合反応後半に反応
系に仕込まれる様にするか、重合反応中に仕込み速度を
漸増させるかして、重合体の お外殻部を形成する重合体中のエポキシ基含有量を多く
させる。良く知られている様に、塩化ビニルの重合体は
単量体(塩化ビニル)に溶解せず、重合反応により発生
した重合体は、単量体液中に析出してくる。従って、重
合反応の後半に、エポキシ基を有する単量体を仕込む様
にすると、エポキシ基を多く含む重合体を外殻部とする
重合体の粒子及びその集合体が、懸濁重合や塊状重合で
は得られる。特に単量体液WJ径が、1μ内外であるミ
クロ懸濁重合では、この構造が顕著である。また、乳化
重合では、重合中における重合反応の場は、常に水と接
する重合体表面であるから、エポキシ基を有する単量体
を重合反応後半に仕込むことで本発明の樹脂を得ること
ができる。
In order to obtain the resin of the present invention using these polymerization methods, the monomer having an epoxy group is charged into the reaction system in the latter half of the polymerization reaction, or the charging rate is gradually increased during the polymerization reaction. In this way, the content of epoxy groups in the polymer forming the outer shell of the polymer is increased. As is well known, a vinyl chloride polymer does not dissolve in a monomer (vinyl chloride), and the polymer generated by the polymerization reaction precipitates in the monomer liquid. Therefore, if a monomer having an epoxy group is introduced in the latter half of the polymerization reaction, polymer particles and aggregates thereof having an outer shell made of a polymer containing a large amount of epoxy groups will undergo suspension polymerization or bulk polymerization. So you can get it. This structure is particularly noticeable in microsuspension polymerization in which the monomer liquid WJ diameter is around 1 μm. In addition, in emulsion polymerization, the site of the polymerization reaction during polymerization is the polymer surface that is always in contact with water, so the resin of the present invention can be obtained by adding a monomer having an epoxy group in the latter half of the polymerization reaction. .

本発明の樹脂の外殻部のエポキシ基含有量は、0.1〜
5重景重量好ましく、0.1重量%以下では、ガラスへ
の接着強度が不充分であるし、5重量%より多いと、耐
貫通性とのバランスが取りにくい。
The epoxy group content of the outer shell of the resin of the present invention is 0.1 to
If the weight is less than 0.1% by weight, the adhesive strength to glass will be insufficient, and if it is more than 5% by weight, it will be difficult to balance the penetration resistance.

やゲル化に過大な熱を要し、製造費用を高める結果とな
る。
Excessive heat is required for gelation and gelation, resulting in increased manufacturing costs.

本発明の塩化ビニル樹脂には目的に応して、可塑剤、安
定剤、紫外線吸収剤、酸化防止剤、滑剤、充填剤、着色
剤などが混合される。さらに、別の塩化ビニル樹脂、ア
クリル樹脂、エポキシ樹脂などの塩化ビニルと相溶しう
る樹脂の混合も可能である。
The vinyl chloride resin of the present invention may be mixed with plasticizers, stabilizers, ultraviolet absorbers, antioxidants, lubricants, fillers, colorants, etc., depending on the purpose. Furthermore, it is also possible to mix resins that are compatible with vinyl chloride, such as other vinyl chloride resins, acrylic resins, and epoxy resins.

配合される可塑剤は一般にポリ塩化ビニル用可塑剤と称
されているものが広く使用できる。
A wide variety of plasticizers that are generally called plasticizers for polyvinyl chloride can be used.

例えば、脂肪族系可塑剤としてはジオクチルアジペート
、ブチルジグリコールアジベート、ジオクチルアゼレー
ト、ジブチルセバケート、アジピン酸ジイソデシル等が
あげられ、フタル酸系可塑剤としてはジオクチルフタレ
ート、ジブヂルフタレー1〜、シイツブデルフタレート
、ブチルヘンジルフタレート、ジラウリルフタレート、
ジオクチルフタレート等があげられ、リン酸系可塑剤と
してはトリキシレニルホスフェート、トリクレジルホス
フェート、タレジルジフェニルホスフェ−1・、1−リ
スクロロエチルホスフェ−1・、トリスクl:I LJ
エチルホスファイト、トリブチルホスフェート等があげ
られる。エポキシ誘導体としてはエポキシ化大豆油、エ
ポキシ脂肪酸モノエステル等がある。
For example, aliphatic plasticizers include dioctyl adipate, butyl diglycol adivate, dioctyl azelate, dibutyl sebacate, diisodecyl adipate, etc., and phthalic acid plasticizers include dioctyl phthalate, dibutyl phthalate 1-, and Delphthalate, butylhenzyl phthalate, dilauryl phthalate,
Examples of phosphoric acid plasticizers include dioctyl phthalate, and examples of phosphoric acid plasticizers include tricylenyl phosphate, tricresyl phosphate, talesyl diphenyl phosphate-1.
Examples include ethyl phosphite and tributyl phosphate. Examples of epoxy derivatives include epoxidized soybean oil and epoxy fatty acid monoester.

ポリエステル系可塑剤も場合によっては使用可能である
。可塑剤の配合量は塩化ビニル系樹脂100重量部に刻
し、20〜80重量部が適当である。
Polyester plasticizers can also be used in some cases. The appropriate amount of plasticizer to be added is 20 to 80 parts by weight, based on 100 parts by weight of the vinyl chloride resin.

可塑剤が多過ぎると膜強度が低下し、少なすぎると硬く
なってしまう。
If there is too much plasticizer, the film strength will decrease, and if it is too little, it will become hard.

熱安定剤としてはブチル錫ラウレート、ブチル錫マレー
ト、オクチル錫マレート等の脂肪酸のアルキル化錫化合
物や、ジノルマルオクチル錫のビス(イソオクチルチオ
グリコール酸エステル)塩等のアルキル錫含有硫黄化合
物が好適に用いられる。これらと共に金属石けん系の安
定剤を併用することも可能である。
Suitable heat stabilizers include alkylated tin compounds of fatty acids such as butyltin laurate, butyltin maleate, and octyltin maleate, and alkyltin-containing sulfur compounds such as di-normal octyltin bis(isooctylthioglycolic acid ester) salt. used for. It is also possible to use a metal soap type stabilizer together with these.

紫外線吸収剤としてはヘンシトリアゾール系が優れてお
り、例えば2(2′−ヒドロキシ−5′メチルフエニル
)ペン申トリアゾール、2(2′ヒドロキシ−3′−タ
ーシャリ−ブチル−5′メチルフエニル)−5−クロロ
ベンゾトリアゾール、2(2′−ヒドロキシ−3’ 、
5’ −ターシャリ−ブチルフェニル)−5−クロロ−
ペンツトリアゾール、2(2′−ヒドロキシル4′−オ
クトキシフエニル)ベンゾI−リアゾール等が好適に用
いられる。
As ultraviolet absorbers, hensitriazoles are excellent, such as 2(2'-hydroxy-5'methylphenyl)benstriazole, 2(2'hydroxy-3'-tert-butyl-5'methylphenyl)-5-chloro Benzotriazole, 2(2'-hydroxy-3',
5'-tert-butylphenyl)-5-chloro-
Penztriazole, 2(2'-hydroxyl 4'-octoxyphenyl)benzo I-riazole and the like are preferably used.

酸化防止剤としてはフェノール系酸化防止剤が優れてお
り、例えば2,6−ジターシャリ−ブチルp−クレゾー
ル、2,2′−メチレンビス(4メチル−6−ターシャ
リ−ブチルフェノール)、4.4′−ブヂリデンビス(
3−メチル−6−ターシャリープチルフェノール)、4
,4′ −チオビス(3−メチル−6−ターシャリープ
チルフェノール)等があげられる。
Phenolic antioxidants are excellent as antioxidants, such as 2,6-ditertiary-butyl p-cresol, 2,2'-methylenebis(4methyl-6-tertiary-butylphenol), and 4,4'-butylidenebis. (
3-methyl-6-tert-butylphenol), 4
, 4'-thiobis(3-methyl-6-tertiarybutylphenol), and the like.

さらに必要に応じ、架橋剤、増粘剤、希釈剤、シラン系
やヂタネート系のカップリング剤などが配合される。
Furthermore, if necessary, a crosslinking agent, a thickener, a diluent, a silane type or ditanate type coupling agent, etc. are blended.

本発明の塩化ビニル樹脂を用いて合せガラスを製造する
には従来から行われている製膜後、ガラスの間にはさみ
、加圧加熱する方法がある。一方、より生産性の高い新
しい製造方法として公開特許公報昭63−134539
の方法がある。この方法の場合、ペースト加工でよく知
られている方法、たとえば本発明の塩化ビニル樹脂に可
塑剤、安定剤、紫外線吸収剤、酸化防止剤等の配合剤を
加え、混合、脱泡する方法などでプラスチゾルを調製す
る。プラスチゾルは液体として取扱えるため、ゴミ・異
物の除去はフィルターなどを通ずだけで行えるし、保管
・輸送もタンク、パイプラインといった閉鎖系で行える
ため、品質管理が容易で自動連続化にも適している。こ
の様なプラスチゾルをガラス板の間に充填し、通常のペ
ースト加工で用いられる加熱装置により、プラスチゾル
層をゲル化し、合せガラスと蘂る。ここで、ガラスに接
するのは粒子の外殻部のため、外殻部に接着成分となる
エポキシ基が多く存在すれば高い接着強度を有すること
が出来る。また、プラスチゾルに充填時に気泡が入らな
いようにしているため、オートクレーブ等の加圧装置が
不必要となる。
In order to manufacture laminated glass using the vinyl chloride resin of the present invention, there is a conventional method of forming a film and then sandwiching it between glasses and heating under pressure. On the other hand, as a new manufacturing method with higher productivity, published patent publication No. 63-134539
There is a method. In the case of this method, a well-known method for paste processing is used, such as a method in which compounding agents such as plasticizers, stabilizers, ultraviolet absorbers, and antioxidants are added to the vinyl chloride resin of the present invention, mixed, and defoamed. Prepare plastisol. Since plastisol can be handled as a liquid, dust and foreign matter can be removed by simply passing it through a filter, and storage and transportation can be done in a closed system such as a tank or pipeline, making quality control easy and suitable for automated continuous use. ing. Such plastisol is filled between glass plates, and the plastisol layer is gelled using a heating device used in normal paste processing, and then laminated with glass. Here, since it is the outer shell of the particle that comes into contact with the glass, high adhesive strength can be achieved if there are many epoxy groups serving as an adhesive component in the outer shell. Furthermore, since air bubbles are prevented from entering the plastisol during filling, a pressurizing device such as an autoclave is not required.

0 (発明の効果) かくして本発明によれば、従来の技術に比較して、接着
強度と耐貫通性に優れた合せガラス用塩化ビニル樹脂を
得ることができる。
0 (Effects of the Invention) Thus, according to the present invention, it is possible to obtain a vinyl chloride resin for laminated glass that has superior adhesive strength and penetration resistance compared to conventional techniques.

(実施例) 以下に実施例を挙げて本発明をさらに具体的に説明する
。なお、実施例、比較例中の部及び%はとくに断りのな
いかぎり重量基準である。
(Example) The present invention will be described in more detail with reference to Examples below. Note that parts and percentages in Examples and Comparative Examples are based on weight unless otherwise specified.

実施例1 10012のステンレス製オートクレーブに脱イオン水
160部、ジオクチルスルホサクシネートナトリウム0
.4部、ラウリルアルコール1部、ラウロイルパーオキ
サイド0.4部を仕込んで減圧脱気後、塩化ビニル97
部を仕込んで、攪拌下にエマルジョンを得た。この混合
物をホモジナイザーで均質化し、別の脱気された100
0 I!、オートクレーブ中に移し45°Cに昇温しで
重合を開始した。昇温後5時間目には重合率が61%に
なっていたので、この時よりグリシジルメタクリレ−1
3部を3時間にわたって、連続的に重合中のオートクレ
ーブ1 に注入して、10時間後に重合を終了させた。未反応の
単量体を減圧回収した後、反応液をスプレー乾燥機によ
り乾燥し、粉砕して樹脂を得た。
Example 1 In a 10012 stainless steel autoclave, 160 parts of deionized water and 0 parts of dioctyl sulfosuccinate sodium were added.
.. After adding 4 parts of lauryl alcohol, 1 part of lauryl alcohol, and 0.4 parts of lauroyl peroxide and degassing under reduced pressure, vinyl chloride 97.
1 part to obtain an emulsion under stirring. This mixture was homogenized with a homogenizer and separated with another degassed 100
0 I! The mixture was then transferred to an autoclave and heated to 45°C to initiate polymerization. Five hours after the temperature was raised, the polymerization rate was 61%, so from this point on, glycidyl methacrylate-1
Three parts were continuously injected into autoclave 1 during polymerization over a period of 3 hours, and the polymerization was terminated after 10 hours. After recovering unreacted monomers under reduced pressure, the reaction solution was dried using a spray dryer and pulverized to obtain a resin.

この樹脂100部にジオクチルアジペート45部、ジオ
クチルフタレート15部、ジブチル錫ポリメルカプタイ
ド4部、2,2′ −メチレンビス(4−メチル−6−
ターシャリ−ブチルフェノール)0.3部をホバートミ
キサー中で混合、減圧脱泡してプラスチゾルを得た。こ
のプラスチゾルを15c+nX 10cm、厚さ3mm
のガラス板にドクターブレードにより塗布し、その上に
厚さ20μmのポリエチレンテレフタレートフィルムを
気泡が人ヤで らない様にのモソ、200 ’Cで15分間加熱し厚さ
0.8mmの樹脂層を有するバイレイヤガラスのを得た
。又、このプラスチゾルを30cmX30cm。
To 100 parts of this resin, 45 parts of dioctyl adipate, 15 parts of dioctyl phthalate, 4 parts of dibutyltin polymercaptide, 2,2'-methylenebis(4-methyl-6-
0.3 part of tertiary-butylphenol was mixed in a Hobart mixer and defoamed under reduced pressure to obtain plastisol. This plastisol is 15c+nX 10cm, thickness 3mm
A 20 μm thick polyethylene terephthalate film was applied on a glass plate using a doctor blade, and then a 0.8 mm thick resin layer was heated at 200°C for 15 minutes to prevent air bubbles from appearing. Obtained bi-layer glass. Also, this plastisol is 30cm x 30cm.

厚さ3n+mのガラス板にロールコータ−で塗布し、さ
らにその上30cmX30cm、厚さ3■のガラス板を
気泡が入らない様に静かにのせ、200°Cで15分間
加熱し、厚さ6.8 mmの合せガラスの2枚を得た。
The coating was applied to a 3n+m thick glass plate using a roll coater, and then a 30cm x 30cm, 3cm thick glass plate was gently placed on top of it, taking care not to introduce air bubbles, and heated at 200°C for 15 minutes. Two sheets of 8 mm laminated glass were obtained.

2 実施例2 1000 ffiのステンレス製オートクレーブに脱イ
オン水160部、ジオクチルスルホサクシネートナトリ
ウム0.4部、ラウリルアルコール1部、ラウロイルパ
ーオキサイド0.4部を仕込んで減圧脱気後、塩化ビニ
ル94部、塩化アリル3部を仕込んで攪拌下にエマルジ
ョンを得た。この混合物をホモジナイザーで均質化して
別の脱気された1000j2オートクレーブ中に移し、
52°Cに昇温しで重合を開始した。以下、実施例1の
ジオクチルアジペート45部、ジオクチルフタレート1
5部をジオすチルアジパー130部サコクチルフタレー
ト10部にした他は実施例1と同様に操作し、パイレイ
ヤーガラス■と合せガラス■2枚とを得た。
2 Example 2 160 parts of deionized water, 0.4 parts of sodium dioctyl sulfosuccinate, 1 part of lauryl alcohol, and 0.4 parts of lauroyl peroxide were placed in a 1000 ffi stainless steel autoclave, and after degassing under reduced pressure, 94% of vinyl chloride was prepared. 1 part and 3 parts of allyl chloride were charged to obtain an emulsion with stirring. The mixture was homogenized with a homogenizer and transferred into another degassed 1000j2 autoclave,
Polymerization was initiated by raising the temperature to 52°C. Below, 45 parts of dioctyl adipate of Example 1, 1 part of dioctyl phthalate
The procedure was repeated in the same manner as in Example 1, except that 5 parts were changed to 130 parts of dioxyl adiper and 10 parts of sucoctyl phthalate, to obtain a pie layer glass (2) and two sheets of laminated glass (2).

実施例3 1000 ffiのステンレス製オートクレーブに脱イ
オン水160部、ジオクチルスルホサクシネートナトリ
ウム0.4部、ラウリルアルコール1部、ラウロイルパ
ーオキサイド0.4部を仕込んで減圧脱気後、塩化ビニ
ル96.5部を仕込んで、攪拌下に工3 マルジョンを得た。この混合物をホモジナイザーで均質
化して、別の脱気された1000 ffiオートクレー
ブ中に移し45°Cに昇温しで重合を開始した。
Example 3 160 parts of deionized water, 0.4 parts of sodium dioctyl sulfosuccinate, 1 part of lauryl alcohol, and 0.4 parts of lauroyl peroxide were placed in a 1000 ffi stainless steel autoclave, and after degassing under reduced pressure, 96% of vinyl chloride was dissolved. 5 parts were charged, and a third emulsion was obtained under stirring. The mixture was homogenized using a homogenizer, transferred to another degassed 1000 ffi autoclave, and heated to 45°C to initiate polymerization.

重合開始時から6時間目にかけてグリシジルメタクリレ
ート1.5部を注入し、6時間目から8時間目にかけて
、グリシジルメタクリレ−12部を注入して、10時間
後に重合を終了させた。以下、実施例1と同様に操作し
、パイレイヤーガラス■と合せガラス■2枚とを得た。
1.5 parts of glycidyl methacrylate was injected from the start of polymerization to 6 hours, 12 parts of glycidyl methacrylate was injected from 6 to 8 hours, and the polymerization was terminated 10 hours later. Thereafter, operations were carried out in the same manner as in Example 1 to obtain pie layer glass (2) and two pieces of laminated glass (2).

実施例4 クメンハイドロパーオキサイドlog、、t−ブチルハ
イドロパーオキサイド10g、ラウリル硫酸ナトリウム
500 g、脱イオン水10kgを高速攪拌機で混合し
てハイドロパーオキサイドエマルジョンを調製した。ま
た、ラウリル硫酸ナトリウム1.6 kg、脱イオン水
28.5 kgを混合して乳化剤水溶液を調製した。
Example 4 A hydroperoxide emulsion was prepared by mixing log of cumene hydroperoxide, 10 g of t-butyl hydroperoxide, 500 g of sodium lauryl sulfate, and 10 kg of deionized water using a high-speed stirrer. Further, an emulsifier aqueous solution was prepared by mixing 1.6 kg of sodium lauryl sulfate and 28.5 kg of deionized water.

さて、10001のステンレス製オートクレーブに脱イ
オン水325kg、平均粒径0.45μmの塩化ビニル
単独重合体樹脂粒子30重量パーセントを4 含むラテックス50kg、R−アスコルビン酸150g
、第一鉄イオンのエチレンジアミン四酢酸ナトリウム醋
塩6g、ピロリン酸ソーダ2.5 kgを仕込み、窒素
置換、減圧脱気を各2回行った。その後塩化ビニル35
7.5 kgを仕込んで内容物を攪拌しながらオートク
レーブのジャケットより加温し、内容物の温度を50°
Cに到達せしめてから、乳化剤水溶液及びハイドロパー
オキサイド・エマルジョンを反応系内δこ各々2.81
!/hr、11!/hrのレートで導入しつつ反応温度
を50°Cに維持した。乳化剤水溶液は同じレートで1
0.5時間導入して停止したが、ハイドロパーオキサイ
ド・エマルジョンは6時間経過して反応転化率が40.
5%の時点で0.71/hrのレートに切換えるととも
にグリシジルメタクリレートを3kg/hrのレートで
15.9kgを注入した。こうして全反応時間12時間
IO分で反応を終了とし冷却した。反応転化率は91.
3%であった。冷却と共にラウリル硫酸ナトリウム0、
5 kg及びポリオキシエチレンソルビタンモノステア
レート1.Okgを脱イオン水10kgに溶解して5 系内に注入してから未反応の単量体を回収した。
Now, in a 10001 stainless steel autoclave, 325 kg of deionized water, 50 kg of latex containing 30 weight percent of vinyl chloride homopolymer resin particles with an average particle size of 0.45 μm, and 150 g of R-ascorbic acid.
, 6 g of ferrous ion sodium ethylenediaminetetraacetic acid salt, and 2.5 kg of sodium pyrophosphate were charged, and nitrogen substitution and vacuum degassing were performed twice each. Then vinyl chloride 35
Charge 7.5 kg and heat the contents from the jacket of the autoclave while stirring to bring the temperature of the contents to 50°.
After reaching C, the emulsifier aqueous solution and the hydroperoxide emulsion were added to the reaction system with δ of 2.81 each.
! /hr, 11! The reaction temperature was maintained at 50°C while introducing at a rate of /hr. The emulsifier aqueous solution is 1 at the same rate.
The hydroperoxide emulsion was introduced for 0.5 hours and then stopped, but after 6 hours, the reaction conversion rate of the hydroperoxide emulsion was 40.
At the 5% point, the rate was switched to 0.71/hr and 15.9 kg of glycidyl methacrylate was injected at a rate of 3 kg/hr. In this manner, the reaction was completed after a total reaction time of 12 hours and 10 minutes, and the mixture was cooled. The reaction conversion rate was 91.
It was 3%. With cooling, sodium lauryl sulfate 0,
5 kg and polyoxyethylene sorbitan monostearate 1. After dissolving Okg in 10 kg of deionized water and injecting the solution into the 5 system, unreacted monomer was recovered.

以下実施例1と同様に操作し、ハイレイヤーガラス■と
合せガラス■2枚とを得た。
Thereafter, operations were carried out in the same manner as in Example 1 to obtain two pieces of high layer glass (■) and two sheets of laminated glass (■).

比較例1 実施例1で昇温後5時間後からグリシジルメタクリレー
トを注入したのを昇温直後から8時間にわたって連続的
に注入した他は実施例1と同様に操作し、バイレイヤガ
ラス■と合せガラス■2枚を得た。
Comparative Example 1 The same procedure as in Example 1 was carried out except that glycidyl methacrylate was injected 5 hours after the temperature was raised in Example 1, but was continuously injected for 8 hours immediately after the temperature was raised, and combined with the bilayer glass ■. Two pieces of glass were obtained.

比較例2 市販の合せガラス用中間膜(ポリビニルブチラール製、
厚さ30n+il)を0.5wt%の水分になるように
調湿し、30cmX30cm、厚さ3mmのガラス板の
上に上記の調湿した中間膜、厚さ20μmのポリエチレ
ンテレフタレートフィルム、30cmX30cm、厚さ
31のカバーガラスの順で積層した(積層体l)。この
積層体1をラバーバッグに入れ、バッグの中を減圧し、
120°Cで30分間保持し、予備圧着を行った。同様
にして、30cmX30cm、厚さ3mmのガラス板2
枚の間に上記の6 調湿した中間膜をはさみ、ラバーバッグを用いて4因 予備圧着を行い、積層体2.2牧を得た。次に積層体1
,2を空気圧式オートクレーブで140°C1■3〜1
5kg/cm”の条件で30分間加圧加熱圧着を行った
。最後に積層体Jのカバーガラスを取りはずし、パイレ
イヤーガラス■寺合せガラス板2枚を得た。
Comparative Example 2 Commercially available interlayer film for laminated glass (made of polyvinyl butyral,
30n+il) was adjusted to have a moisture content of 0.5wt%, and placed on a 30cm x 30cm, 3mm thick glass plate was the above humidity controlled interlayer film, a 20μm thick polyethylene terephthalate film, 30cm x 30cm, thickness 31 cover glasses were laminated in this order (laminate I). Put this laminate 1 into a rubber bag, reduce the pressure inside the bag,
Preliminary pressure bonding was performed by holding at 120°C for 30 minutes. Similarly, a glass plate 2 of 30cm x 30cm and 3mm thick
The above humidity-controlled interlayer film 6 was sandwiched between the sheets, and 4-factor preliminary pressure bonding was performed using a rubber bag to obtain a laminate of 2.2 mm. Next, laminate 1
, 2 in a pneumatic autoclave at 140°C 1 ■ 3 ~ 1
Pressure and heat compression bonding was carried out for 30 minutes at a pressure of 5 kg/cm''.Finally, the cover glass of the laminate J was removed to obtain two laminated glass plates made of pie layer glass.

実施例1〜3及び比較例1〜2で得られた合せガラスの
性能を調べるためJIS−R−3212r自動車安全ガ
ラスの試験方法Jに準拠した下記の方法により透明性、
耐貫通強度、耐衝撃性、接着強度を測定し、その結果を
表に示した。
In order to investigate the performance of the laminated glass obtained in Examples 1 to 3 and Comparative Examples 1 to 2, transparency and
The penetration resistance, impact resistance, and adhesive strength were measured, and the results are shown in the table.

1、透明性(可視光線透過率) 合せガラス■〜■を分光光度計(日立製作所製)で38
0nmから750nmまでの透過率を測定した。
1. Transparency (visible light transmittance) Laminated glass ■~■ was measured with a spectrophotometer (manufactured by Hitachi, Ltd.) at 38
Transmittance was measured from 0 nm to 750 nm.

2、耐貫通強度 透明性を測定した合せガラス■〜■を20 ’Cの雰囲
気下で2時間放置後この合せガラスの中心に2.27k
gの鋼球を4mの高さから落下させ、貫通7 の有無を見る。
2. After leaving the laminated glass ■~■ whose penetration resistance strength and transparency were measured in an atmosphere of 20'C for 2 hours, a 2.27k mark was placed in the center of this laminated glass.
Drop a steel ball g from a height of 4 m and check whether there is any penetration 7.

3、耐衝撃性 もう−枚の合せガラス■〜■を23°Cの雰囲気下で2
時間放置後、227gの鋼球を9mの高さから落下させ
、衝撃面の反対側からはくすしたガラスの総重量を測定
した。
3. Impact resistance - Laminated glass sheets ■~■ under an atmosphere of 23°C.
After standing for a period of time, a 227 g steel ball was dropped from a height of 9 m, and the total weight of the smoldered glass was measured from the opposite side of the impact surface.

4、接着強度 パイレイヤーガラス■〜■を23°Cの雰囲気下で2時
間放置後、中間膜の部分を一部はがし300mm/mi
nのスピードでTピール接着強度を測定する。
4. Adhesive strength After leaving the Pylayer glass ■~■ in an atmosphere at 23°C for 2 hours, part of the interlayer film was peeled off and bonded at 300mm/mi.
Measure the T-peel adhesive strength at a speed of n.

評価結果を表に示す。表より、本発明による合せガラス
は、合せガラスの性能を満足させることができる。
The evaluation results are shown in the table. From the table, the laminated glass according to the present invention can satisfy the performance of laminated glass.

8 ■ 98 ■ 9

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

第1図及び第2図は電子顕微鏡による粒子の断面写真で
、これらより粒子構造を知ることができる。即ち、第1
図は実施例1により得られた粒子の断面を示すものでエ
ポキシ基を含む粒子外層部ゆ がルテニウム酸より黒く染められている。一方、第2図
は比較例1により得られた粒子に同し処理を施したもの
で、粒子全体がほぼ同様の明度でありエポキシ基が粒子
全体にほぼ均一に分布していることが判る。
FIGS. 1 and 2 are cross-sectional photographs of particles taken using an electron microscope, and the structure of the particles can be understood from these photographs. That is, the first
The figure shows a cross section of the particles obtained in Example 1, in which the outer layer of the particles containing epoxy groups is dyed darker than the ruthenic acid. On the other hand, FIG. 2 shows the particles obtained in Comparative Example 1 subjected to the same treatment, and it can be seen that the entire particles have approximately the same brightness and the epoxy groups are distributed almost uniformly throughout the particles.

Claims (2)

【特許請求の範囲】[Claims] (1)粒径が5μ以下で粒子の外殻部のエポキシ基含有
量が粒子の中核部のエポキシ基含有量より高いことを特
徴とする粒子、及びその集合体からなる合せガラス用塩
化ビニル樹脂
(1) A vinyl chloride resin for laminated glass consisting of particles and aggregates thereof, which have a particle size of 5 μm or less and have a higher epoxy group content in the outer shell than in the core of the particles.
(2)塩化ビニルとエポキシ基を有する単量体と任意成
分であるこれらと共重合可能な単量体との共重合体から
なることを特徴とする特許請求の範囲第1項記載の合せ
ガラス用塩化ビニル樹脂
(2) The laminated glass according to claim 1, which is made of a copolymer of vinyl chloride, a monomer having an epoxy group, and an optional monomer copolymerizable with these. vinyl chloride resin
JP11647789A 1989-05-10 1989-05-10 Method for producing vinyl chloride resin for laminated glass interlayer Expired - Lifetime JP2779832B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP11647789A JP2779832B2 (en) 1989-05-10 1989-05-10 Method for producing vinyl chloride resin for laminated glass interlayer
EP19900304929 EP0397439B1 (en) 1989-05-10 1990-05-08 Vinyl chloride resin for safety glass and process for preparation of the resin
DE69017748T DE69017748T2 (en) 1989-05-10 1990-05-08 Vinyl chloride resin for safety glass and process for producing the resin.
US07/520,426 US5091487A (en) 1989-05-10 1990-05-08 Vinyl chloride resin for safety glass and process for preparation of the resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11647789A JP2779832B2 (en) 1989-05-10 1989-05-10 Method for producing vinyl chloride resin for laminated glass interlayer

Publications (2)

Publication Number Publication Date
JPH0362840A true JPH0362840A (en) 1991-03-18
JP2779832B2 JP2779832B2 (en) 1998-07-23

Family

ID=14688075

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11647789A Expired - Lifetime JP2779832B2 (en) 1989-05-10 1989-05-10 Method for producing vinyl chloride resin for laminated glass interlayer

Country Status (1)

Country Link
JP (1) JP2779832B2 (en)

Also Published As

Publication number Publication date
JP2779832B2 (en) 1998-07-23

Similar Documents

Publication Publication Date Title
EP0020159B1 (en) Composition for interlayer film of laminated safety glass, and laminated safety glass comprising such interlayer film
US4999071A (en) Process for manufacturing laminated safety glass
JPH03126648A (en) Laminated glass manufacturing method and equipment
EP0397439B1 (en) Vinyl chloride resin for safety glass and process for preparation of the resin
JPH047308A (en) Preparation of vinyl chloride resin for laminated glass
JPH11511195A (en) Copolymer of vinyl chloride, allyl glycidyl ether and vinyl ester and method for producing the same
JPH0362840A (en) Vinyl chloride resin for laminated glass
JPH07172878A (en) Intermediate film for laminated glass
JPH03126646A (en) Method and device for producing laminated glass
JPH0280354A (en) Interlayer film composition for laminated glass
JPH0365542A (en) Manufacturing method of laminated glass
EP0385716B1 (en) Process for production of safety glass
EP0389208A1 (en) Interlayer for laminated safety glass
JPH02302345A (en) Manufacturing method of laminated glass
JPH02217341A (en) Manufacturing method of laminated glass
JPH03164452A (en) Production of safety sandwich glass plate
JP2802431B2 (en) Manufacturing method of laminated glass
JPH0453827B2 (en)
JPH04149043A (en) Production of sandwich glass
JPH0730199B2 (en) Method for producing vinyl chloride resin foam
JPH0388839A (en) Intermediate film composition for safety glass and intermediate film for safety glass using same composition
JPH03126647A (en) Laminated glass manufacturing method and equipment
JPS6215497B2 (en)
JPH03169543A (en) Synthetic resin-glass laminate
JPH03122035A (en) Patterned laminated glass plate and its manufacturing method