JPS5857406A - Production of polyvinyl butyral having improved autohesion - Google Patents
Production of polyvinyl butyral having improved autohesionInfo
- Publication number
- JPS5857406A JPS5857406A JP15547481A JP15547481A JPS5857406A JP S5857406 A JPS5857406 A JP S5857406A JP 15547481 A JP15547481 A JP 15547481A JP 15547481 A JP15547481 A JP 15547481A JP S5857406 A JPS5857406 A JP S5857406A
- Authority
- JP
- Japan
- Prior art keywords
- polyvinyl butyral
- polyvinyl
- acid
- temperature
- added
- 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.)
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- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はポリビニルブチラールの製造方法に関し、詳し
くは、可m荊を加えて合せガクス用中岡膜を製造すると
常温における中間膜同志の粘着性(以下中間膜の自着性
という。)が大巾に改善された合せガラス用中陶屓が得
られるポリビニルブチラール01!造方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing polyvinyl butyral, and more specifically, when a Nakaoka membrane for laminated gas is produced by adding a polyvinyl butyral, the adhesiveness of the interlayer films at room temperature (hereinafter referred to as self-adhesion of the interlayer film) Polyvinyl butyral 01 allows you to obtain a medium ceramic for laminated glass that has greatly improved It is related to the manufacturing method.
今日、広く工業的に利用されているポリビニルブチラー
ルO製沫は沈澱法と溶解法とに大別される。この内沈澱
法は、例えば、酸触媒の存在下でポリビニルアルコール
の水溶液にメチルアルデヒドを加え20℃以下の比較的
低温度でブチクール化反応を行いポリビニルグチフール
の微細沈澱を生ぜしめ九徒、更に長時ll攪拌、加熱す
る方法である。又溶解法は、例えばイソプロピルアルコ
ール等の有機溶剤中に、11’ IJビニルアルコール
を分数させ酸触媒の存在下にグチルアルデヒドを加えて
加熱し長時間反応させる方法である。Polyvinyl butyral O sludge, which is widely used industrially today, can be roughly divided into precipitation methods and dissolution methods. In this internal precipitation method, for example, methylaldehyde is added to an aqueous solution of polyvinyl alcohol in the presence of an acid catalyst and a butycooling reaction is carried out at a relatively low temperature below 20°C to produce fine precipitates of polyvinylgutifur. This method involves stirring and heating for a long time. The dissolution method is, for example, a method in which a fraction of 11' IJ vinyl alcohol is added to an organic solvent such as isopropyl alcohol, gtyraldehyde is added in the presence of an acid catalyst, and the mixture is heated and reacted for a long period of time.
然し乍ら、これら従来の方法によって製造されたポリビ
ニルブチラールKjJ塑剤を加えて得られ九合せガラス
用中**F!、**面の粘着性が強い1製W11のm同
時KM同志が粘着するという問題を有し、かかる粘着を
防ぐ為に膜表面に重lR111ソーダ410粘着防止剤
を散布した)、20℃以下の温度に中間膜を冷即するこ
とが行なわれて−る。However, polyvinyl butyral KjJ produced by these conventional methods can be obtained by adding a plasticizer for use in laminated glass. , ** There was a problem that the 1-made W11 m simultaneous KM comrades with strong adhesion stuck to each other, and to prevent such adhesion, a heavy lR111 soda 410 anti-stick agent was sprayed on the membrane surface), below 20 ° C. The interlayer film is cooled to a temperature of .
しかし粘着防止剤を散布する方法はポリビニルブチラー
ル膜とガラスとを接着するIIK、事前に粘着防止削除
*O為の水洗工程及び乾燥工程を経なければならないと
いう1iiAを有し、ま九冷凍法は中間膜の製造から包
装、輸送、保存そして使用時まで冷凍装置が必要であ夛
高価につくという難点を有し、実質的に常温における自
着性が無い中間膜の出現が待たれていた。However, the method of spraying the anti-adhesion agent has IIK, which involves bonding the polyvinyl butyral film and glass, and 1IIA, which requires a washing process and drying process to remove the anti-adhesion in advance. The interlayer film has the drawback that it requires a refrigeration system from production to packaging, transportation, storage, and use, making it very expensive, and the emergence of an interlayer film that is substantially free of self-adhesion at room temperature has been awaited.
本発明はポリビニルブチラールの製造方法の上述の現状
に鑑み、得られ九ボリビニルグチラールに可塑剤を加え
て合せガラス用中間膜を製造すると自着性が大巾に改善
され九合せガラス用中間膜が得られるポリビニルグチク
ールの製造方法を提供することを目的とするもので、そ
の要旨は、ポリビニルアルコールのアセタール化により
得られたポリビニルブチラールを水相中に分数させた賦
型で、塩酸、臭化水素酸及び硝酸のそれぞれ0水潜性填
O少くとも1つの存在下に強酸性領域で30℃以上の温
度に保つことを特徴とする自着性か改善され喪ポリビニ
ルブチラールoH造方法に存する。In view of the above-mentioned current state of the method for producing polyvinyl butyral, the present invention has been proposed to produce an interlayer film for laminated glass by adding a plasticizer to the obtained polyvinyl butyral, and the self-adhesion is greatly improved. The purpose of this is to provide a method for producing polyvinylguticool that can obtain a membrane, and its gist is to form a fraction of polyvinyl butyral obtained by acetalizing polyvinyl alcohol into an aqueous phase, and to prepare a polyvinyl butyral film using hydrochloric acid, A process for producing polyvinyl butyral OH with improved self-adhesive properties, characterized by maintaining the temperature at 30°C or higher in a strongly acidic region in the presence of at least one of hydrobromic acid and nitric acid, each with zero water latent filler O. Exists.
本発明に供されるポリビニルグチクールはポリビニルア
ルコールのアセタール化により得られ大もので6れば出
発原料がポリビニルアセテートであってもよく、可塑剤
を加えると自着性を有する中間膜を形成する一〇が広く
使用される。しかし水相中に分散させるので、同様に本
相中で製造したポリビニルブチラールを用いるのが好ま
しい。この場合に工業的に特に好ましいのは、酸触媒の
存在下でポリビニルアルコールとブチルアルデヒドとを
反応させてポリビニルブチツールを水相中で沈澱析出せ
しめた後、該Il脂を反15系から分離することなくそ
のまま同じ水相中で後!&理することである。しかし、
上記沈澱法や溶解法4IO従米公知の方法により得られ
九乾燥したポリビニルグチクール粉末の使用も勿論可能
である。The polyvinylguticool used in the present invention is obtained by acetalizing polyvinyl alcohol, and the starting material may be polyvinyl acetate, and when a plasticizer is added, it forms an interlayer film with self-adhesive properties. 10 is widely used. However, since it is dispersed in the aqueous phase, it is preferred to use polyvinyl butyral which is also produced in the main phase. In this case, it is particularly preferred industrially to react polyvinyl alcohol and butyraldehyde in the presence of an acid catalyst to precipitate polyvinyl butitur in the aqueous phase, and then separate the Il fat from the anti-15 system. Afterwards, leave it in the same aqueous phase without any problems! & Understand. but,
Of course, it is also possible to use polyvinyl guccicool powder obtained by the above-mentioned precipitation method or dissolution method 4IO and dried.
本発明に用いるポリビニルグチクールとしては、36℃
以上O温度に保って得られ九ポリビニルブチラールを合
せガラス用中間膜として用いる場合はグチ2−ル化度が
60〜75モル%で小ることが望ましく、又、クン化度
が95モル%以上、叉には98モル%以上のポリビニル
アルコールから製せられたものであとのが、最終絢に透
明性の良好な樹脂が得られる点で好ましい。又このとき
のポリビニルアルコールの平均重合度は、低過ぎると可
塑剤を加えて中間膜とじ九場合O自着性改咎効果が乏し
く、高過ぎると粘度が高くて工業的にアセタール化する
のに不都合であるので、通常Fi800〜300Gのも
のが用いられる。The polyvinyl guchicool used in the present invention has a temperature of 36°C.
When using the polyvinyl butyral obtained by keeping the above O temperature as an interlayer film for laminated glass, it is desirable that the degree of crosslinking is as small as 60 to 75 mol%, and the degree of crosslinking is preferably 95 mol% or more. , or those made from polyvinyl alcohol with a content of 98 mol % or more are preferable in that a resin with good transparency can be obtained in the final fiber. Also, if the average degree of polymerization of polyvinyl alcohol at this time is too low, the effect of improving self-adhesion when binding an interlayer film by adding a plasticizer will be poor; if it is too high, the viscosity will be high and it will be difficult to acetalize it industrially. Since this is inconvenient, one with an Fi of 800 to 300G is usually used.
本発明における塩酸、臭化水素酸及び硝酸のそれぞれの
水溶性塩の好適な例としては、それぞれの&6性成分が
マグネシクム、カルシフ^、亜鉛、アルミ二りム、鉄、
チタン等の2偏重上Ow、子価を有するものが挙けられ
る。これらの樵はそれぞれ単独で又は適宜組合わせて用
−られ、その使用量は通常分数させたポリビニルプ本発
明におけるポリビニルグチクールの分数液濃度は樹脂が
水相中に分散される濃度であれば特に限定されないが、
過113〜ls重量%とされる。この時微量のアルデヒ
ドが上記分散液中に存在していてもよく、その量Fi通
常分分散の1重量%以下とされる。Preferred examples of the water-soluble salts of hydrochloric acid, hydrobromic acid and nitric acid in the present invention include magnesium, calcium, zinc, aluminum, iron,
Examples include those having a valence of 2, such as titanium. These resins are used alone or in appropriate combinations, and the amount used is usually fractional polyvinyl resin.The fractional liquid concentration of polyvinylguticool in the present invention is the concentration at which the resin is dispersed in the aqueous phase. Although not particularly limited,
The content is 113 to 11% by weight. At this time, a trace amount of aldehyde may be present in the dispersion, and the amount is set to be 1% by weight or less of the normal dispersion of Fi.
上記水溶性塩のポリビニルブチラール分散液への添加は
、ポリビニルアルコールのアセタール化後に高温で余り
長時間を経過しない内に行うのが、メリビニルグチクー
ル粒子の粗大化を防止する上で#i?ましい。In order to prevent the coarsening of melivinylguticool particles, it is best to add the above-mentioned water-soluble salt to the polyvinyl butyral dispersion before a too long period of time has elapsed at a high temperature after acetalizing the polyvinyl alcohol. Delicious.
本発明において強酸性領域のポリビニルブチラール分散
液を得るKは、従来公知の高酸、硫酸、硝酸等の無機酸
やパラトルエンスルホン酸等の有機酸を用いて得られた
強酸性本相中に乾燥したポリビニルグチツールを加えて
もよく、前記ポリビニルグチクールを水相に分散してか
らのちに前記酸を加えてもよく、或いは又gII酸性本
相中にポリビニルグチクールを沈澱析出せしめてもよい
。In the present invention, K for obtaining a polyvinyl butyral dispersion in a strongly acidic region is added to a strongly acidic main phase obtained using a conventionally known high acid, an inorganic acid such as sulfuric acid, nitric acid, or an organic acid such as para-toluenesulfonic acid. Dry polyvinylguticool may be added, the acid may be added after the polyvinylguticool is dispersed in the aqueous phase, or the polyvinylguticool may be precipitated into the gII acidic main phase. good.
本発明における強酸性領域とは、ポリビニルグチラーA
/妙欽液O温度にもよるが通常PH2以下とされ、好ま
しく#1PH1以下とされる。The strongly acidic region in the present invention refers to polyvinyl gutilyl A
/Myokin liquid O Although it depends on the temperature, the pH is usually 2 or less, preferably #1 PH1 or less.
又、ポリビニルグチクールのグチツール化度を増大させ
る必要のある鳩舎は、前記分散液中に所定量のグチルア
ルデヒドを存在せしめることKより、ブチラール化の増
大を行うことが出来る。In addition, for pigeon houses where it is necessary to increase the degree of butyralization of polyvinyl butyral, the degree of butyralization can be increased by allowing a predetermined amount of butyraldehyde to be present in the dispersion.
又、ポリビニルブチラールのlII皮0i11度の上限
は特に定められないが一般に90℃以下とされ、30℃
以上の温度に保つ時間は、分散液の外温及び降温の時間
を含め通常は1〜20時間とされる。In addition, the upper limit of the lII skin of polyvinyl butyral is not particularly determined, but it is generally set to 90°C or less, and 30°C
The time for maintaining the above temperature is usually 1 to 20 hours, including the time for the external temperature of the dispersion liquid and the time for cooling the dispersion liquid.
本発明方法によりポリビニルブチラールを製造するKa
、通常は、20℃を越える温度のポリビニルアルコール
本溶液に酸触媒を加え、次いで反I15系を冷却し、ブ
チルアルデヒドを加えて結合反応させてポリビニルブチ
ラールの沈澱を20℃以下の如く低温でV出せしめて、
水相中に分散させたポリビニルブチラールを用意する。Ka for producing polyvinyl butyral by the method of the present invention
Usually, an acid catalyst is added to the main polyvinyl alcohol solution at a temperature of over 20°C, then the anti-I15 system is cooled, and butyraldehyde is added to cause a binding reaction to precipitate polyvinyl butyral at a low temperature such as 20°C or lower. Don't let it out,
Provide polyvinyl butyral dispersed in an aqueous phase.
この様に沈澱析出時に反応系の温度を低く保りOは沈澱
物を微小な粒子状又は粉状で得るためであシ、温度O下
wlは、反6a’&が凍結しなi嫌な温度であればよ(
特に制限されるものではないが、通常−6℃以上O11
度が採用される。In this way, the temperature of the reaction system is kept low during precipitation, and O is used to obtain the precipitate in the form of fine particles or powder. As long as it's the temperature (
Although not particularly limited, usually -6℃ or higher O11
degree is adopted.
次に反応系のPHが2以下O状lで上記樵の少くと41
りを加え反応系を外温し30℃以上の温度に保って反E
t−更に進行せしめた後、触媒を塩基で中和し、反応生
成物を取シ出して常法忙よシ洗浄、精製を行うのである
。Next, if the PH of the reaction system is 2 or less, the above woodcutter is at least 41
The reaction system was heated externally and kept at a temperature of 30°C or higher.
After the reaction has proceeded further, the catalyst is neutralized with a base, and the reaction product is taken out and washed and purified in a conventional manner.
こ0*に、dリピニルアルコールのア七タール化により
得られ九ポリビニルブチクールを水相φに分散させた状
態で、塩酸、臭化水素酸及び硝酸の夫々O水溶性壌O少
くとも1つの存在下に強酸性領域で前記分散液の温度を
30℃以上に保りことにより、呵麿剤を加えて合せガラ
ス用中間膜を製造すると実質的に常温における自着性が
ない中間膜が得られる0であり、こO橡に自着性が改善
されたぼりビニルブチツールが製造される理由につ−で
は未だ充分には明らかではないが、次O31夛推測され
る。In this case, in a state in which 9-polyvinyl buticol obtained by the 7-tarization of d-lipinyl alcohol is dispersed in the aqueous phase φ, at least 1 % of each of hydrochloric acid, hydrobromic acid and nitric acid is added to the water-soluble solution. If an interlayer film for laminated glass is manufactured by adding an analizing agent and maintaining the temperature of the dispersion liquid at 30°C or higher in a strongly acidic region in the presence of a substance, an interlayer film with virtually no self-adhesion at room temperature can be obtained. Although it is not yet fully clear why vinyl butty tools with improved self-adhesive properties are produced in this way, it is speculated that the following reasons may arise.
グチツーに化反I5は平衡反応であるので、反応が成る
程度進行し大平衡状謙において、グチツール化度#iは
は一定となる。従来公知の製造方決では一般に、ブチク
ール化度が一定の状態に達する前に反応を停止していた
のであ夛、こ0時のポリビニルグチクール中0伐水酸基
は2ンダムな配列をしていると考えられる。しかしてこ
Oポリビニルグチテールを水相中に分散させ、上紀樵の
存在下に強酸性領域で前記分散液011度を30℃以上
に保つと、強酸性領域下で生じる逆ブチクール化反応に
より生成する水酸基は水素結合による全台を示す傾向が
あり、一方グチラール化反t)は、食合の傾向の強い水
酸基よりもそうでない水酸基Kjl択的に起り易くなる
。従って最終的平衡状態に近ずくと、分子内に水酸基が
連鎖的に挾る傾向が強ま夛、これによって得られたポリ
ビニルグチクールの剛性が増加し、これが中間膜として
用いられた際の自着性の滅夕すなわち改善に寄与するも
のと考えられる。Since the reaction I5 is an equilibrium reaction, the reaction progresses to the extent that it reaches a state of great equilibrium, and the degree of reaction #i becomes constant. In conventional production methods, the reaction was generally stopped before the degree of butycooling reached a certain level; therefore, the hydroxyl groups in the polyvinyl guccicool at this time were arranged in a random order. it is conceivable that. However, if the lever-O polyvinyl tail is dispersed in an aqueous phase and the dispersion liquid is kept at 30 degrees Celsius or higher in a strongly acidic region in the presence of a woodcutter, the product is formed by a reverse butycooling reaction that occurs in a strongly acidic region. Hydroxyl groups that do tend to exhibit complete hydrogen bonding, while butyralization (t) is more likely to occur selectively for hydroxyl groups that do not have a strong tendency to eclipse than for hydroxyl groups that have a strong tendency to eclipse. Therefore, as the final equilibrium state approaches, the tendency for hydroxyl groups to be chained in the molecule increases, which increases the rigidity of the obtained polyvinylguticool, which increases its self-reliance when used as an interlayer film. It is thought that this contributes to reducing or improving adhesion.
本J1明看等は、上記壌の不存在下でもポリビニルブチ
ラールの分散液を強酸性域で比較的高温で長時間保った
ポリビニルブチツーklc可履則を加えると自着性が改
善され喪中間膜が得られるという知見をすでに得たもの
であるが、本発明における上記塩を使用すると上記温度
及び時間の条件が著しく緩和され工程上有利になるので
ある。This J1 review shows that even in the absence of the above-mentioned soil, self-adhesion is improved by adding polyvinyl butyral dispersion liquid maintained at a relatively high temperature for a long time in a strongly acidic region. Although it has already been found that a film can be obtained, the use of the above-mentioned salt in the present invention significantly relaxes the above-mentioned temperature and time conditions, which is advantageous in terms of the process.
又、例えば沈澱法においてポリビニルグチクールの微細
粒子を析出せしめ死後、上記塩の不存在下ては高温で長
時岡保つと沈澱粒子の凝集等による粗大化が生じ易くな
り、粗大化し九粒子中には酸触媒やその中和に用いた環
基等が残溜して透明性叉にti熱安定性を低下せしめる
値向か6つえが、上記*には微粒子の粗大化を防止する
作用があり透明性や熱安定性を低下せしめることが殆ん
どな−のである。In addition, for example, if fine particles of polyvinylguticool are precipitated in the precipitation method and kept at high temperature for a long time in the absence of the above salt after death, coarsening due to agglomeration of precipitated particles is likely to occur. However, the above * has the effect of preventing the coarsening of fine particles, as the acid catalyst and the ring groups used for its neutralization remain and reduce the transparency and thermal stability of Ti. There is almost no reduction in transparency or thermal stability.
本発明方決により得られたポリビニルグチツールに用い
る呵ll剤は従来よりポリビニルブチクー#O為O可■
剤七して用りられるものをいずれ4使用することかで壷
、伺えばトリエチレングリコ−A/−ジ2エチルブチレ
ート、トリエチレングリコ−#−ジ意エチルヘキソエー
トなどの汎用可塑剤が挙げられる。更にジブトキシジエ
チレングリコールアジペートなどが好適に使用される。The agent used in the polyvinyl butylene tool obtained by the method of the present invention is conventionally used in polyvinyl butylene.
General-purpose plasticizers such as triethylene glyco-A/-di2-ethyl butyrate and triethylene glyco-A/-di-ethylhexoate are commonly used as additives. can be mentioned. Furthermore, dibutoxydiethylene glycol adipate and the like are preferably used.
可塑剤の添加量はポリビニルブチff−に1110重量
1sK対し、30乃至60重量部が!Iましい。可塑剤
が30重量部米満では合せガラス用中間膜とした時の耐
貫通性が低下し、可ll剤が60重量部を越えるものは
可塑剤が膜表面にしみ出すいわゆるブリード現象が生じ
、合わせガラス用中岡膜とした時の透明性及び接着性に
悪影響を1埋すからである。The amount of plasticizer added is 30 to 60 parts by weight per 1110 sK of polyvinyl butylene ff-! I love it. If the plasticizer is 30 parts by weight, the penetration resistance will decrease when used as an interlayer film for laminated glass, and if the plasticizer exceeds 60 parts by weight, a so-called bleed phenomenon will occur in which the plasticizer seeps onto the film surface, resulting in poor lamination. This is because it has an adverse effect on the transparency and adhesiveness when used as a Nakaoka membrane for glass.
本発明方法は上述の遥)の構成になされており、本発明
によれば、可塑剤を加えて合せガラス用中閏屓を製造す
ると常温における自着性が顕著に改善され九合せガラス
用中岡膜が得られるポリビニルブチツールが塩酸、臭化
水素酸及び硝酸のそれぞれの水溶性塩の何れをも用いな
い場6に比較して工業的に有利な温度・時−〇条件下で
得ることができるのである。The method of the present invention has the above-mentioned configuration, and according to the present invention, when a plasticizer is added to produce a middle plate for laminated glass, the self-adhesion at room temperature is significantly improved. The polyvinyl butytool from which the membrane is obtained can be obtained under industrially advantageous temperature and time conditions compared to the case 6 when none of the water-soluble salts of hydrochloric acid, hydrobromic acid, and nitric acid are used. It can be done.
又、本発明において微細なポリビニルブチラール粒子を
用い九鳩舎は、粗大化粒子が殆んど*IIしていない透
明性、II&安定性O喪好なポリビニルブチラールを得
ることができるのである。In addition, in the present invention, by using fine polyvinyl butyral particles, it is possible to obtain polyvinyl butyral with good transparency, high stability, and almost no coarse particles.
以下に本発明の実施例を示す。単に%とあるのは重量%
を意味する。尚、実施例における各物性値轄次の測定法
によった。Examples of the present invention are shown below. % simply means weight %
means. The following measurement methods were used for each physical property value in the examples.
L 透明性
ポリビニルグチクールが二枚のガラス板0111に挾ん
で得られた試料を加熱されたオープン中に入れてポリビ
ニルブチラールを溶融し九IIK室温で放冷した。得ら
れた試料を白色光のもとで観察し、青味、濁り等のない
ものを良好とし・た。A sample obtained by sandwiching the transparent polyvinyl butyral between two glass plates 0111 was placed in a heated open chamber to melt the polyvinyl butyral and allowed to cool at room temperature. The obtained sample was observed under white light, and those without bluishness, turbidity, etc. were evaluated as good.
2 熱安定性
ポリビニルブチテールを入れた試験管を加温され九油i
!に浸し、120℃にて所定時−ヲ経てもメジビニルブ
チツールが変色しない鳩舎を熱安定性が良好であるとし
た。2 A test tube containing thermostable polyvinyl butytail was heated to
! Pigeon houses in which the medivinylbutytool did not change color even after being immersed in water and heated at 120° C. for a predetermined period of time were considered to have good thermal stability.
一般に中和又は水洗が不完全な場合KFiポリビニルブ
チツール中に塩酸等の触媒が跣存し、本試験を行うとポ
リビニルブチツールは黄色に着色する。Generally, if neutralization or washing with water is incomplete, a catalyst such as hydrochloric acid remains in the KFi polyvinyl butytool, and when this test is performed, the polyvinyl buthytool is colored yellow.
亀 自着性
ポリビニルグチツール100重量部tcIvr定の可塑
剤42重量部を加えライカイ機て1s分間混合し、ロー
ルを用い120’CKて1分間混練し九後150℃、4
0即/−にて3分間プレスし表面の平滑な厚さa76M
の均一なフィルムを作成した。ζ0フイルムを3 am
X 1 Oam O長方形状に切り取り、2枚重ね合
わせ・即の荷重をか叶た状1でxo”co温度に保った
デシクーター中にて48時閏麓装した。Add 100 parts by weight of self-adhesive polyvinyl guchi tool and 42 parts by weight of a plasticizer with tcIvr constant, mix for 1 second using a Raikai machine, knead for 1 minute at 120'CK using a roll, and then mix at 150°C for 4 minutes.
Press at 0/- for 3 minutes to obtain a smooth surface with a thickness of a76M.
A uniform film was created. ζ0 film 3 am
X 1 Oam O was cut into a rectangular shape, two sheets were superimposed, and the shape 1, which was immediately loaded, was placed in a desiccator kept at xo''co temperature for 48 hours.
こ01Kして得られた試料の一端を互に剥し、剥され九
フィルムを90℃方向に曲げて全体を丁字形にし死後、
剥されたフィルムの両方の端を引張試験機でつかみ20
’CKて50@調/分O引張速度でTl1ll−強度を
測定した。One end of the sample obtained at 01K was peeled off from each other, and the peeled film was bent in a 90°C direction to form a T-shape.
Grasp both ends of the peeled film with a tensile tester for 20 minutes.
Tl1ll-strength was measured at a tensile rate of 50 m/min.
表 耐衝撃性
〆リビニルグチツーに100重量都K11r履剤42重
量部を添加混騨し、押し出し機にて、厚さα76鱈0W
qIl化ボリビ;ルグチラールを得え、このフィルムを
厚11tO鱈、SOamX3@関Oガ夛ス板2板の岡に
挾み込み、従来公知05kfl−で加熱加圧して合わせ
ガラスを得た。こO合せガラスを所定温度に8時間以上
保管した徒、外枠が31611X31ms内枠が26−
X 26 cm、高さ2 @ alOマス餐鉄枠上に水
平に置も、λ268即(5〆ンド)0m球を指定された
高さから合わぜガラスO中心KlK下させた。Table: Impact resistant finish: Add 42 parts by weight of 100% K11r lubricant to ribinyl rubber, mix and mix with an extruder to a thickness of α76 cod 0W.
A qIl-containing bolibi; lugutilal was obtained, and this film was sandwiched between two 11tO cod, SOam If the laminated glass is kept at the specified temperature for more than 8 hours, the outer frame will be 31611 x 31ms and the inner frame will be 26mm.
X 26 cm, height 2 @ alO Placed horizontally on the iron frame of a mass restaurant, a λ268 (5〆nd) 0m ball was placed from the specified height and lowered to the center of the glass O.
合せガラスを鋼球が貫通する割合がSO−%となる高さ
を耐貫通強度とし次。The height at which the percentage of steel balls penetrating the laminated glass becomes SO-% is defined as the penetration resistance strength.
尚、合せガフスO試粁としてFi、予め壷属石けんを適
宜添加混合した可ffi#を用いることにより後述する
バンメル値を製品として通電便用される1lIl(>6
に毅定したものを用いた。In addition, by using Fi as a combined gaff O test sample and ffi # mixed with a suitable amount of soap in advance, the bummel value described later can be obtained as a product with 1lIl (>6
I used the one that was firmly established.
飄 ガラスに対する接着性 。Adhesiveness to glass.
合せガラスを一り8℃±Q6℃Os1度に16時同波置
して調整し、これを顕Sがa4140ハンマーで打って
ガラ10粒饅が6jI11以下になる迄粉砕した。ガラ
スが剥離し死石の膜の露出度をあらかじめグレード付け
した限度見本で判定し、その結果を第1表に従いパンメ
ル値として表わした。A piece of laminated glass was adjusted to 8℃±Q6℃Os 1 degree by heating at 16:00, and Ken S. pounded it with an A4140 hammer until 10 pieces of glass became 6jI11 or less. The degree of exfoliation of the dead stone film caused by the exfoliation of the glass was determined using limit samples that had been graded in advance, and the results were expressed as pummel values according to Table 1.
第 1 表
実施例1
クン化度916モル%、重合度!10(10ポシビエル
アルフー〜011j6水JII液1@・即に濃塩酸(濃
度3!%)1即を加え、13’CKて攪拌しつつ3・分
岡要してグチルアルデヒドへ7即を滴下し九ところ白色
微粒子状のポリビニルブチクー#O沈澱が析出した。Table 1 Example 1 Degree of conversion: 916 mol%, degree of polymerization! 10 (10Posibiel Alf~011j6 water JII solution 1@・Immediately add 1 portion of concentrated hydrochloric acid (concentration 3!%), 13'CK and stir while stirring 3 minutes. When the mixture was added dropwise, fine white particles of polyvinylbutycous #O were precipitated.
さらに3J11gI6濃填酸7即を加えて攪拌し反応系
OPmlを(L5以下にし、臭化カルレフ^の16%水
溶液las即を加え(臭化力ルシクムの量は最終的に得
られ九ポリビニルグチツール14)0重量部に対して2
0重量部であった。)20℃/時岡O昇温遮度で40′
cまでiI+温し、叉に6時間その温度を保って熟成を
6倉り先後水酸化ナトリクムを加えて反fI5系を中和
しPH*tL@とし九・30℃以上の温度に保つ九時岡
ttts*mであった。Further, 3J11gI6 concentrated acid 7g was added and stirred to bring the reaction system OPml to below L5, and a 16% aqueous solution of Calf bromide was added (the amount of Calf bromide was determined by the final amount obtained). 14) 2 to 0 parts by weight
It was 0 parts by weight. )20℃/40' at Tokioka O temperature increase shielding rate
Warm to iI+ to c, then maintain that temperature for 6 hours to ripen for 6 hours. After 6 hours of aging, add sodium hydroxide to neutralize the anti-fI5 system and make PH*tL@9.Kutokioka, which is kept at a temperature of 30℃ or above. It was ttts*m.
得られた樹脂を常法に従い水洗、乾燥を行ない白色微粉
末を得た。このポリビニルブチツールOグチツール化度
は6へ496でめった。The obtained resin was washed with water and dried according to a conventional method to obtain a white fine powder. The degree of polyvinylbutytool O-butytoolization was 6 to 496.
この嫌にして得られたポリビニルブチツール、該ポリビ
ニルブチクール1001fに可塑剤としてトリエチレン
グリ2−ルージ2エチルブチレート42却を加えて得ら
れ九中閏膜及び該中間層から得られた合せガラスの物性
は第2表に示す過少であった。The polyvinyl butytool obtained by this process, the polyvinyl butycoal 1001f obtained by adding triethylene glycol 2-rouge 2-ethyl butyrate 42 as a plasticizer, and the intermediate layer obtained from the The physical properties of the glass were as shown in Table 2.
実施例2
実施例Iにおいて臭化カルシタムC1代すに種化第二鉄
を用りた以外は全て実施例1と岡IKしてポリビニルブ
チラールの粉゛末を得た。Example 2 A polyvinyl butyral powder was obtained by repeating the same procedure as in Example 1 except that ferric seeding was used instead of calcium bromide C1 in Example I.
その物性等Fi第2麦に示す通りであった。Its physical properties were as shown in Fi No. 2.
実施例3
実施例1と同様にして反J6系中に白色微粒しめた。さ
らに臭化カルレフ^の代りに臭化マグネシクムを加えた
のち60℃に昇温してその温度に3時間保った以外は実
施例1と同様にしてポリビニルブチクールの粉末を得た
。Example 3 In the same manner as in Example 1, white fine particles were packed in anti-J6 system. Furthermore, a powder of polyvinyl buticool was obtained in the same manner as in Example 1, except that magnesium bromide was added instead of Calref^ bromide, and then the temperature was raised to 60°C and kept at that temperature for 3 hours.
その物性勢は第2麦に示す通りであった。Its physical properties were as shown in the second barley.
実施例4
実施例1において臭化カルシタムの代シに硝酸亜鉛を用
いた以外は全て実施例1とW4様にしてポリビニルブチ
ラールO粉末を得た。Example 4 Polyvinyl butyral O powder was obtained in the same manner as in Example 1 and W4 except that zinc nitrate was used in place of calcium bromide.
その物性4Iは第21に示す通りであった。Its physical properties 4I were as shown in No. 21.
実施例5
ケン化度99.6モル%、重合度21000ポリビニル
アルコールの13%水溶液100r4に濃塩酸(濃度3
5%)l即を加え13℃にて攪拌しつつグチルアルデヒ
ドa7Qを30分周要して加えたところ白色微粒子状の
ポリビニルブチラールO沈鹸が得られた。さらに濃塩酸
7F4を加え反応系を攪拌しつつ20℃/1時IIO昇
温速度で40℃まで昇温してその温度に3時間保った彼
、常法により中和、水洗工程を経てブチラール化度65
.8モル%、σ
平均粒径17−声の乾燥したポリビニルブチラールを程
良。Example 5 Concentrated hydrochloric acid (concentration 3
5%) was added thereto, and while stirring at 13° C., gtyraldehyde a7Q was added over a period of 30 minutes to obtain polyvinyl butyral O precipitate in the form of white fine particles. Furthermore, he added concentrated hydrochloric acid 7F4, stirred the reaction system, raised the temperature to 40°C at a rate of 20°C/1 hour IIO temperature increase, and kept it at that temperature for 3 hours.He then neutralized it using a conventional method and converted it to butyral through a water washing process. degree 65
.. 8 mol%, σ average particle size 17 - Moderately dry polyvinyl butyral.
臭化亜鉛012g6水溶液&4峙に濃度35%O樵酸6
F4を加え上記乾燥メジビニルグチツール10即を分数
させ(分数液のPHはα5以下であった。)、該分数液
を48℃にて5時間保つ&彼、水酸化ナトリクムを加え
て中和しrat−asとし以下実施例1と同様にしてポ
リビニルグチクールの粉末を得た。その物性等は第21
kに示す通りであった。Zinc bromide 012g 6 aqueous solution & 4 sides 35% O citric acid 6
F4 was added to fractionate 10 pieces of the dried mejivinylgutitool (the pH of the fraction was less than α5), and the fraction was kept at 48°C for 5 hours and neutralized by adding sodium hydroxide. A powder of polyvinyl Guchicool was obtained in the same manner as in Example 1 using rat-as. Its physical properties etc. are the 21st
It was as shown in k.
比較例1
実施例五において臭化力ルンクムを加えない以外はすで
て実施例1と同様にしてポリビニルグチクールの粉末を
得た。その物性◆は第2表に示す過シであった。Comparative Example 1 A powder of polyvinylguchicool was obtained in the same manner as in Example 1, except that no bromide was added in Example 5. Its physical properties ◆ were as shown in Table 2.
比較例2
実施例3において臭化マグネシクムを加えない以外はす
べて実施例3と同様にしてポリビニルグチクールの粉末
を得た。その物性曽は第2麦に示す通りであった。Comparative Example 2 Polyvinyl Guticool powder was obtained in the same manner as in Example 3 except that magnesium bromide was not added. Its physical properties were as shown in the second barley.
比較例3
実施例5において臭化亜鉛を用いない以外はすべて実施
例5と同様にして後段のポリビニルブチラールO粉末を
得た。その物性*Fi第2表に示す通りであった。Comparative Example 3 Polyvinyl butyral O powder in the latter stage was obtained in the same manner as in Example 5 except that zinc bromide was not used. Its physical properties *Fi were as shown in Table 2.
Claims (1)
たポリビニルグチクールを水相中に分数させた吠■で、
mal1%臭化水素酸及び硝酸のそれぞれの水溶性塩
O少くとも1′)0存在下に強酸性領域で30℃以上の
温度に保つことを特徴とする自着性が改善されたポリビ
ニルグチツーkOIl造方法。 λ 水溶性塩の量が分散液中のポリビニルグチラールt
ool量部に対し0重量部以上である亜鉛、アルミニタ
ム、鉄、チタンのうちの少くとも1つである第1項又は
第2項記載の製造方法。 435℃以上の温度に保り時間が1〜20時崗で6る第
1項〜ll3JJll何れかIJJK記載の製造方法。 敷 強酸性領域のPHが2以上である第1項〜第4Jj
[何れか111K記載の製造方法。 亀 アセタール化により得られたポリビニルグチクール
を、反15系から分離することなく同じ水相ゆで熟成す
る111項〜第51i4何れかIJJK記軌O製造方法
。[Scope of Claims] L A polyvinylguticool obtained by acetalization of polyvinyl alcohol-kO is fractionated into an aqueous phase,
A polyvinyl glutinous resin with improved self-adhesive properties, characterized in that it is maintained at a temperature of 30°C or higher in a strongly acidic region in the presence of at least 1% water-soluble salts of hydrobromic acid and nitric acid. kOIl production method. λ The amount of water-soluble salt in the dispersion of polyvinylgtyralt
The manufacturing method according to item 1 or 2, wherein the amount of at least one of zinc, aluminum, iron, and titanium is 0 parts by weight or more based on the amount of ool. The manufacturing method according to any one of Items 1 to 13JJK, wherein the temperature is maintained at 435°C or higher for a time of 1 to 20 hours. Items 1 to 4 Jj where the pH of the strongly acidic region is 2 or more
[Any manufacturing method described in 111K. Kame A method for producing any of IJJK Kiki O, which comprises boiling and aging polyvinylguchicool obtained by acetalization in the same aqueous phase without separating it from the anti-15 system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15547481A JPS5857406A (en) | 1981-09-29 | 1981-09-29 | Production of polyvinyl butyral having improved autohesion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15547481A JPS5857406A (en) | 1981-09-29 | 1981-09-29 | Production of polyvinyl butyral having improved autohesion |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5857406A true JPS5857406A (en) | 1983-04-05 |
| JPH0114922B2 JPH0114922B2 (en) | 1989-03-15 |
Family
ID=15606834
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15547481A Granted JPS5857406A (en) | 1981-09-29 | 1981-09-29 | Production of polyvinyl butyral having improved autohesion |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5857406A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6483024A (en) * | 1987-09-25 | 1989-03-28 | Kyukyu Yakuhin Kogyo Kk | Cataplasm for cold |
| US7674854B2 (en) * | 2004-08-04 | 2010-03-09 | Sekisui Chemical Co., Ltd. | Process for producing polyvinyl acetal resin, polyvinyl butyral resin, and process for producing esterified polyvinyl alcohol resin |
-
1981
- 1981-09-29 JP JP15547481A patent/JPS5857406A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6483024A (en) * | 1987-09-25 | 1989-03-28 | Kyukyu Yakuhin Kogyo Kk | Cataplasm for cold |
| US7674854B2 (en) * | 2004-08-04 | 2010-03-09 | Sekisui Chemical Co., Ltd. | Process for producing polyvinyl acetal resin, polyvinyl butyral resin, and process for producing esterified polyvinyl alcohol resin |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0114922B2 (en) | 1989-03-15 |
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