JPS6053042B2 - Method for producing polyvinyl butyral - Google Patents

Method for producing polyvinyl butyral

Info

Publication number
JPS6053042B2
JPS6053042B2 JP8305881A JP8305881A JPS6053042B2 JP S6053042 B2 JPS6053042 B2 JP S6053042B2 JP 8305881 A JP8305881 A JP 8305881A JP 8305881 A JP8305881 A JP 8305881A JP S6053042 B2 JPS6053042 B2 JP S6053042B2
Authority
JP
Japan
Prior art keywords
polyvinyl butyral
temperature
perchloric acid
reaction system
laminated glass
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP8305881A
Other languages
Japanese (ja)
Other versions
JPS57195706A (en
Inventor
茂 野村
正志 宮川
研一 朝比奈
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP8305881A priority Critical patent/JPS6053042B2/en
Publication of JPS57195706A publication Critical patent/JPS57195706A/en
Publication of JPS6053042B2 publication Critical patent/JPS6053042B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B17/00Layered products essentially comprising sheet glass, or glass, slag, or like fibres
    • B32B17/06Layered products essentially comprising sheet glass, or glass, slag, or like fibres comprising glass as the main or only constituent of a layer, next to another layer of a specific material
    • B32B17/10Layered products essentially comprising sheet glass, or glass, slag, or like fibres comprising glass as the main or only constituent of a layer, next to another layer of a specific material of synthetic resin
    • B32B17/10005Layered products essentially comprising sheet glass, or glass, slag, or like fibres comprising glass as the main or only constituent of a layer, next to another layer of a specific material of synthetic resin laminated safety glass or glazing
    • B32B17/1055Layered products essentially comprising sheet glass, or glass, slag, or like fibres comprising glass as the main or only constituent of a layer, next to another layer of a specific material of synthetic resin laminated safety glass or glazing characterized by the resin layer, i.e. interlayer
    • B32B17/10761Layered products essentially comprising sheet glass, or glass, slag, or like fibres comprising glass as the main or only constituent of a layer, next to another layer of a specific material of synthetic resin laminated safety glass or glazing characterized by the resin layer, i.e. interlayer containing vinyl acetal

Landscapes

  • Joining Of Glass To Other Materials (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

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、透明性、熱安定性にすぐれ、可塑剤を加えて合
せガラス用中間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間膜が得られるポリビニルブチラー
ルの製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, it has excellent transparency and thermal stability, and when an interlayer film for laminated glass is produced by adding a plasticizer, the interlayer films have a high adhesiveness to each other at room temperature. The present invention relates to a method for producing polyvinyl butyral that provides an interlayer film for laminated glass with greatly improved self-adhesion properties (hereinafter referred to as interlayer film self-adhesion).

ポリビニルブチラールの製法として広く工業的に利用
されている沈澱法は、例えば酸触媒の存在下にポリビニ
ルアルコールの水溶液にブチルアルデヒドを加え20℃
以下の比較的低温領域で縮合反応を起させてポリビニル
ブチラールの微細沈澱を生ぜしめ、その後所定のブチラ
ール化度を得る為に反応系を昇温し、20℃乃至40℃
の温度にて長時間保つ方法が一般的である。
The precipitation method, which is widely used industrially to produce polyvinyl butyral, is, for example, adding butyraldehyde to an aqueous solution of polyvinyl alcohol in the presence of an acid catalyst at 20°C.
A condensation reaction is caused in the following relatively low temperature range to produce fine precipitates of polyvinyl butyral, and then the temperature of the reaction system is raised to obtain a predetermined degree of butyralization from 20°C to 40°C.
A common method is to maintain the temperature for a long period of time.

然し乍ら、従来の方法によつて製造されたポリビニル
ブチラールに可塑剤を加えて得られた合せガラス用中間
膜は、膜表面の粘着性が強い為製膜後の捲回時に膜同志
が粘着するという問題を有し、かかる粘着を防ぐ為に膜
表面に重炭酸ソーダ等の粘着防止剤を散布したり、20
℃以下の温度に中間膜を冷却することが行なわれている
However, the interlayer film for laminated glass obtained by adding a plasticizer to polyvinyl butyral produced by the conventional method has a strong adhesive surface, which causes the films to stick to each other when being rolled after film formation. In order to prevent such adhesion, anti-adhesive agents such as bicarbonate of soda are sprayed on the membrane surface, and
The interlayer film is cooled to a temperature below .degree.

しカル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際に、事前に粘着防止剤除
去の為の水洗工程及ひ乾燥工程を経なければならないと
いう難点を有し、また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り高価
につくという難点を有し、常温における自着性の無い中
間膜の出現が待たれていた。
The method of spraying an anti-adhesive agent has the disadvantage that it requires a washing process and a drying process to remove the anti-adhesive agent before bonding the polyvinyl butyral film and glass. The process ranges from interlayer film production to packaging,
This method requires a refrigeration system for transportation, storage, and use, and is expensive, so the emergence of an interlayer film that does not self-adhere at room temperature has been awaited.

本発明は上述の現状に鑑み、透明性、熱安定性にすぐ
れ、得られたポリビニルブ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
た合せガラス用中間膜が得られるポリビニルブチラール
の製造方法を提供することを目的とするもので、その要
旨は酸触媒の存在下に水相中でポリビニルアルコールと
ブチルアルデヒドを縮合せしめてポリビニルブチラール
を製造する方法において、反応系を20℃以下の温度に
保つて沈澱物を析出せしめたのち昇温し、過塩素酸系化
合物の存在下で、反応系を30′C以上の温度に保つて
熱成させることを特徴とするポリビニルブチラールの製
造方法に存する。
In view of the above-mentioned current situation, the present invention has been developed for laminated glass, which has excellent transparency and thermal stability, and whose self-adhesiveness is greatly improved when an interlayer film for laminated glass is produced by adding a plasticizer to the obtained polyvinyl butyral. The purpose of this invention is to provide a method for producing polyvinyl butyral from which an interlayer film can be obtained, and the gist thereof is a method for producing polyvinyl butyral by condensing polyvinyl alcohol and butyraldehyde in an aqueous phase in the presence of an acid catalyst. , the reaction system is maintained at a temperature of 20°C or lower to precipitate a precipitate, and then the temperature is raised, and the reaction system is maintained at a temperature of 30'C or higher in the presence of a perchloric acid compound for thermal formation. The present invention is characterized by a method for producing polyvinyl butyral.

本発明において用いられるポリビニルアルコールの平均
重合度は800〜3000が好適であり、またそのケン
化度は透明性の良いポリビニルブチラールを得る為に好
ましくは95モル%以上、特に好適には部モル%以上で
ある。
The average degree of polymerization of the polyvinyl alcohol used in the present invention is preferably 800 to 3000, and the degree of saponification is preferably 95 mol% or more, particularly preferably part mol%, in order to obtain polyvinyl butyral with good transparency. That's all.

ポリビニルアルコールの水溶液濃度はアセタール化反応
を行うことが出来る濃度であれば特に限定されないが通
常3乃至1鍾量%とされる。本発明に用いられる酸触媒
についてはポリビニルアルコールとブチルアルデヒドを
縮合せしめる作用を有することが知られている酸を適宜
用いることができ、例えば硫酸、硝酸、塩酸等の無機酸
やバラトルエンスルホン酸等の有機酸が挙げられる。
The concentration of the aqueous solution of polyvinyl alcohol is not particularly limited as long as it can carry out the acetalization reaction, but it is usually 3 to 1% by weight. As for the acid catalyst used in the present invention, acids known to have the effect of condensing polyvinyl alcohol and butyraldehyde can be appropriately used, such as inorganic acids such as sulfuric acid, nitric acid, and hydrochloric acid, and valatoluenesulfonic acid. Examples include organic acids.

酸触媒の使用量は、反応の最終時における濃度が0.5
乃至5重量%となる量が望ましい。触媒は所要量を一度
に添加しても良いが、微細なポリビニルブチラールを沈
澱析出せしめる為には適当な回数に分割添加するのが好
ましい。例えば塩酸の場合は、沈澱物の析出前に全所要
重量の1/20−乃至1/3を添加し残りを沈澱物の析
出後に添加するのが好ましい。本発明においてポリビニ
ルアルコールと縮合せしめるブチルアルデヒドの使用量
は目的とするポリビニルブチラールのブチラール化度に
応じて適.宜決定されるが、ポリビニルブチラールを合
せガラス用中間膜に用いる場合はブチラール化度が60
乃至75モル%であることが望ましくその為にはポリビ
ニルアルコール10踵量部に対し、豹部乃至74部のブ
チルアルデヒドを加えるのが好適であ−る。本発明にお
ける過塩素酸系化合物とは過塩素酸及びその塩を意味し
、過塩素酸塩の好適な例としては、過塩素酸ナトリウム
、過塩素酸カリウム等のアルカリ金属塩や過塩素酸マグ
ネシウム、過塩素酸カルシウム等のアルカリ土類金属塩
が挙げられ、特に過塩素酸ナトリウムが好適である。
The amount of acid catalyst used is such that the concentration at the end of the reaction is 0.5.
A desirable amount is 5% by weight. The required amount of catalyst may be added at once, but in order to precipitate fine polyvinyl butyral, it is preferable to add the catalyst in portions at appropriate times. For example, in the case of hydrochloric acid, it is preferable to add 1/20 to 1/3 of the total required weight before precipitation, and add the remainder after precipitation. In the present invention, the amount of butyraldehyde condensed with polyvinyl alcohol is appropriate depending on the desired degree of butyralization of polyvinyl butyral. However, when polyvinyl butyral is used as an interlayer film for laminated glass, the degree of butyralization is 60.
It is desirable that the amount is from 75 mol% to 75 mol%, and for that purpose it is preferable to add 74 parts of butyraldehyde to 10 parts of polyvinyl alcohol. The perchloric acid compound in the present invention refers to perchloric acid and its salts. Preferred examples of perchlorates include alkali metal salts such as sodium perchlorate and potassium perchlorate, and magnesium perchlorate. and alkaline earth metal salts such as calcium perchlorate, with sodium perchlorate being particularly preferred.

これら過塩素酸系化合物は、夫々単独で又は組合わせて
用いられ、その使用量は最終系において0.2〜1踵量
%となる量が通常用いられるが、この量に制限されるも
のではない。又過塩素酸系化合物を反応系に加える時期
は、ポリビニルブチラールの沈澱物が析出する前からl
沈澱物の析出後反応系を30℃以上の温度に昇温した直
後迄の間であればいつでも良いが、通常は反応開始時に
ブチルアルデヒドをいまだ加えていないポリビニルアル
コール水溶液に酸触媒と共に添゛加するのがよい。
These perchloric acid compounds are used alone or in combination, and the amount used is usually 0.2 to 1% by weight in the final system, but is not limited to this amount. do not have. Also, the time to add perchloric acid compound to the reaction system is from before the precipitation of polyvinyl butyral.
Although it can be done at any time immediately after the reaction system is heated to a temperature of 30°C or higher after the precipitation of the precipitate, butyraldehyde is usually added to the polyvinyl alcohol aqueous solution to which it has not yet been added together with an acid catalyst at the start of the reaction. It is better to do so.

本発明方法によりポリビニルブチラールを製造するには
、通常は、200を越える温度のポリビニルアルコール
水溶液に酸触媒を加え、次いで上記過塩素酸系化合物を
加えた後反応系を冷却し、ブチルアルデヒドを加えて縮
合反応させてポリビニルブチラールの沈澱を20℃以下
の温度で析出せしめる。
To produce polyvinyl butyral by the method of the present invention, an acid catalyst is usually added to an aqueous polyvinyl alcohol solution at a temperature of over 200°C, then the above perchloric acid compound is added, the reaction system is cooled, and butyraldehyde is added. A condensation reaction is carried out to precipitate polyvinyl butyral at a temperature of 20° C. or lower.

この様に沈澱析出時に反応系の温度を低く保つのは沈澱
物を微小な粒子状又は粉状で得るためである。
The reason why the temperature of the reaction system is kept low during precipitation is to obtain the precipitate in the form of fine particles or powder.

20′C以下における温度の下限は、反応系が凍結しな
い様な温度であればよく特に制限されるものではないが
、通常−6℃以上の温度が採用される。
The lower limit of the temperature below 20'C is not particularly limited as long as the reaction system does not freeze, but a temperature of -6C or above is usually employed.

次にポリビニルブチラールの沈澱析出後、通常は過塩素
酸系化合物の存在下に、反応系を昇温し30℃以上の温
度に保つて反応を更に進行せしめて熱成を行つた後、酸
触媒を塩基で中和し、反応生成物を取り出して常法によ
り洗浄、精製を行うのである。
Next, after precipitation of polyvinyl butyral, the temperature of the reaction system is raised and maintained at a temperature of 30°C or higher to further advance the reaction, usually in the presence of a perchloric acid compound. The reaction product is neutralized with a base, and the reaction product is extracted and washed and purified using conventional methods.

熱成時における温度の上限は特に定められるものではな
いがアルデヒドの過度の蒸発を防止する為に9(代)以
下の温度が好ましく、又熱成時間も特に定められるもの
ではないが通常1時間乃至1時間とされる。
The upper limit of the temperature during thermal formation is not particularly determined, but in order to prevent excessive evaporation of the aldehyde, a temperature of 9 or below is preferable, and the thermal formation time is also not particularly specified, but is usually 1 hour. It is said to last from 1 hour to 1 hour.

この様に、2CfC以下の温度で沈澱物を析出させた後
上記過塩素酸系化合物の存在下で反応系を30℃以上の
温度に保つて熱成することにより、透明性、熱安定性に
すぐれたポリビニルブチラールが得られ、該ポリビニル
ブチラールを可塑化すると自着性等の性質が改善された
中間膜が得られる理由については未だ充分には明らかで
はないが、上記過塩素酸系化合物の存在下で熱成される
ことにより、ポリビニルアルコール中の水酸基が連鎖的
に配列した水素結合による会合の傾向の強い部分よりも
他の部分へのブチラール化反応が選択的に起り易くなり
、最終的には、分子内に水酸基が連鎖的に残る傾向が強
まり、これによつて得られたポリビニルブチラールの剛
性が増加し、これが自着性の減少に寄与するものと考え
られる。
In this way, transparency and thermal stability can be improved by precipitating a precipitate at a temperature of 2CfC or less and then thermally forming it by keeping the reaction system at a temperature of 30°C or more in the presence of the above-mentioned perchloric acid compound. Although the reason why excellent polyvinyl butyral can be obtained and why an interlayer film with improved properties such as self-adhesion can be obtained by plasticizing the polyvinyl butyral is still not fully clear, the presence of the above-mentioned perchloric acid compound By thermally forming the hydroxyl groups in polyvinyl alcohol, the butyralization reaction is more likely to occur selectively in other parts than in parts where the hydroxyl groups in polyvinyl alcohol have a strong tendency to associate due to hydrogen bonds arranged in a chain. It is thought that this increases the tendency for hydroxyl groups to remain in a chain in the molecule, thereby increasing the rigidity of the obtained polyvinyl butyral, which contributes to a decrease in self-adhesion.

又、透明性や熱安定性に関しては、本発明者等は、上記
過塩素酸系化合物の不存在下でも沈澱物の熱成を比較的
高温且つ長時間行うことにより自着性が改善される中間
膜が得られるという知見を得たが、この場合沈澱粒子の
凝集等による粗大化が生じ易くなり、粗大化した粒子中
には酸触媒やその中和に用いた塩基等が残溜して透明性
更には熱安定性を低下せしめる傾傾向があつた。これに
対し、上記過塩素酸系化合物が2CfC以下の温度で沈
澱析出させた微粒子の粗大化を防止する作用を有する為
に、本発明においては最終的に透明性及び熱安定性にす
ぐれたポリビニルブチラールが得られるものと考えられ
る。本発明方法により得られたポリビニルブチラールに
用いる可塑剤は従来よりポリビニルブチラールの為の可
塑剤として用いられるものをいずれも使用することがで
き、例えばトリエチレングリコールニジ2エチルブチレ
ート、トリエチレングリコールニジ2エチルヘキソエー
トなどが好適に使用される。
In addition, regarding transparency and thermal stability, the present inventors have found that self-adhesion is improved by thermally forming the precipitate at a relatively high temperature and for a long time even in the absence of the above-mentioned perchloric acid compound. We have found that an interlayer film can be obtained, but in this case, the precipitated particles tend to become coarse due to agglomeration, and the acid catalyst and the base used for its neutralization remain in the coarse particles. There was a tendency for transparency and thermal stability to decrease. On the other hand, since the above-mentioned perchloric acid compound has the effect of preventing the coarsening of the fine particles precipitated at a temperature of 2 CfC or lower, in the present invention, the final product is polyvinyl which has excellent transparency and thermal stability. It is believed that butyral is obtained. The plasticizer used for the polyvinyl butyral obtained by the method of the present invention can be any of those conventionally used as plasticizers for polyvinyl butyral, such as triethylene glycol di-2-ethyl butyrate, triethylene glycol di-2-ethyl butyrate, triethylene glycol di-2-ethyl butyrate, triethylene glycol di-2-ethyl butyrate, 2-ethylhexoate and the like are preferably used.

可塑剤の添加量はポリビニルブチラール100重量部に
対し、30乃至60重量部が望ましい。可塑剤が3轍量
部未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、可塑剤が6踵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、合せガラス用
中間膜とした時の透明性及び接着性に悪影響を及ぼすか
らである。本発明方法は上述の通りの構成になされてお
り、反応系を2(代)以下の温度に保つて沈澱物を析出
させた後昇温し、上記過塩素酸系化合物の存在下で反応
系を3CfC以上の温度に保つて熱成させるので本発明
によれば、粗大化粒子が殆んど含まれす酸触媒や塩基等
の成分が粗大化粒子中に残溜することがないので透明性
、熱安定性にすぐれたポリビニルブチラールが得られ、
又該ポリビニルブ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顕著に改善された合せガ
ラス用中間膜が得られ、更に該中間膜を用いれば耐衛性
にすぐれた合せガラスが得られるのである。
The amount of plasticizer added is preferably 30 to 60 parts by weight per 100 parts by weight of polyvinyl butyral. If the amount of plasticizer is less than 3 parts, the penetration resistance will decrease when used as an interlayer film for laminated glass, and if the amount of plasticizer is more than 6 parts, the so-called bleed phenomenon will occur where the plasticizer seeps onto the film surface. This is because it adversely affects transparency and adhesiveness when used as an interlayer film for laminated glass. The method of the present invention is constructed as described above, in which the reaction system is maintained at a temperature of 2 or below to precipitate a precipitate, and then the temperature is raised, and the reaction system is heated in the presence of the above-mentioned perchloric acid compound. According to the present invention, since the particles are thermally formed by maintaining the particles at a temperature of 3CfC or higher, components such as acid catalysts and bases, which are mostly contained in the coarse particles, do not remain in the coarse particles, resulting in transparency. , polyvinyl butyral with excellent thermal stability is obtained,
Furthermore, when an interlayer film for laminated glass is produced by adding a plasticizer to the polyvinyl butyral, an interlayer film for laminated glass with significantly improved self-adhesion can be obtained, and furthermore, if this interlayer film is used, a laminated glass film with excellent sanitary resistance can be obtained. Glass is obtained.

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は次の測定法
によつた。1粘度分布 ポリビニルブチラール100fを4,16,28,48
,60,80,100の各メッシュ数の篩で分級し、各
篩上に残つた樹脂の重量から測定した。
Examples of the present invention are shown below. % simply means weight %
means. In addition, each physical property value in Examples was based on the following measuring method. 1 viscosity distribution polyvinyl butyral 100f 4, 16, 28, 48
, 60, 80, and 100 mesh numbers, and the weight of the resin remaining on each sieve was measured.

2透明性 ポリビニルブチラール30yを二枚の10(3角のガラ
ス板の間に挾んで得られた試料を160℃の温度に保た
れたオープン中に5分間入れてポリビニルブチラールを
溶融した後に室温で放冷した。
2 A sample obtained by sandwiching transparent polyvinyl butyral 30y between two 10 (triangular glass plates) was placed in an open chamber kept at a temperature of 160°C for 5 minutes to melt the polyvinyl butyral, and then allowed to cool at room temperature. did.

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。3熱安定性ポリビニルブチラー
ル1yを入れた試験管を加温された油浴に浸し、120
℃にて5時間を経てもポリビニルブチラールが変色しな
い場合を熱安定性が良好であるとした。
The obtained sample was observed under white light, and those without bluishness, turbidity, etc. were evaluated as good. 3 Immerse a test tube containing thermostable polyvinyl butyral 1y in a heated oil bath,
A case where the polyvinyl butyral did not change color even after 5 hours at ℃ was considered to have good thermal stability.

一般に中和又は水洗が不完全な場合にはポリビニルブチ
ラール中に塩酸等の触媒が残存し、本試験を行うとポリ
ビニルブチラールは黄色に着色する。
Generally, when neutralization or water washing is incomplete, catalysts such as hydrochloric acid remain in polyvinyl butyral, and when this test is performed, polyvinyl butyral is colored yellow.

4自着性 ポリビニルブチラール10濾量部に所定の可塑剤4鍾量
部を加えライカイ機で1紛間混合し、ロールを用い12
0Cにて3分間混練した後1500C140k9/Cl
tにて3分間ブレスし表面の平滑な厚さ0.76?の均
一なフィルムを作成した。
4 Add 4 parts of a predetermined plasticizer to 10 parts of self-adhesive polyvinyl butyral, mix into 1 powder using a Raikai machine, and mix using a roll for 12 parts.
After kneading for 3 minutes at 0C, 1500C140k9/Cl
Press at t for 3 minutes and the surface will have a smooth thickness of 0.76? A uniform film was created.

このフィルムを30X1?の長方形状に切り取り、2枚
重ね合わせ6k9の荷重をかけた状態で2(代)の温度
に保つたデシケ−ター中にて4時間放置した。この様に
して得られた試料の一端を互に剥し、剥されたフィルム
を900方向に曲げて全体をT字形にした後、剥された
フィルムの両方の端を引張・試験機でつかみ2C)Cに
て500m/分の引張速度で90験剥離強度を測定した
Is this film 30X1? It was cut into a rectangular shape, and two sheets were placed one on top of the other and left in a desiccator kept at a temperature of 200° C. under a load of 6k9 for 4 hours. One end of the sample obtained in this way is peeled off from each other, the peeled film is bent in a 900 direction to make the whole into a T shape, and both ends of the peeled film are grabbed with a tensile/testing machine 2C) 90 test peel strength was measured at a tensile speed of 500 m/min.

5耐衝撃性 ポリビニルブチラール10鍾量部に可塑剤42重量部を
添加混練し、押し出し機にて、厚さ0.76T!f!R
の可塑化ポリビニルブチラールを得た。
5. Add and knead 42 parts by weight of plasticizer to 10 parts by weight of impact-resistant polyvinyl butyral, and use an extruder to obtain a thickness of 0.76T! f! R
A plasticized polyvinyl butyral was obtained.

このフィルムを厚さ3.0m130C71×30dのガ
ラス板2枚の間に挾み込み、温度12C)C1圧力12
kg/dの条件で1紛間加熱加圧して合せガラスを得た
。この合せガラスを所定温度に8時間以上保管した後、
外枠が31(7ft×31d1内枠が2泗×2泗、高さ
2hのマス型鉄枠上に水平に置き、2.268kg(5
ボンド)の鋼球を指定された高さから合わせガラスの中
心に落下させた。合せガラスを鋼球が貫通する割合が5
0%となる高さを耐貫通強度とした。
This film was sandwiched between two glass plates with a thickness of 3.0 m, 130 C, and 71 x 30 d.
One powder was heated and pressed under the conditions of kg/d to obtain a laminated glass. After storing this laminated glass at a specified temperature for more than 8 hours,
The outer frame is 31 (7 ft.
A steel ball (bond) was dropped from a specified height onto the center of the laminated glass. The percentage of steel balls penetrating laminated glass is 5
The height at which the value was 0% was defined as the penetration resistance strength.

尚、合せガラスの試料としては、予め金属石けんを適宜
量添加混合した可塑剤を用いることにより後述するパン
メル値を製品として通常使用される範囲の6に設定した
ものを用いた。
The laminated glass sample used was one in which the pummel value, which will be described later, was set to 6, which is within the range normally used as a product, by using a plasticizer mixed with an appropriate amount of metal soap.

6ガラスに対する接着性 合せガラスを−1(代)±0.6℃の温度にf時間放置
して調整し、これを頭部が0.45kgのハンマーで打
つてガラスの粒径が61a以下になる迄粉砕した。
6 Adhesion to Glass Laminated glass was adjusted by leaving it at a temperature of -1 (s) ± 0.6°C for f hours, and then struck with a hammer with a head weighing 0.45 kg until the particle size of the glass was 61a or less. I smashed it until it became.

ガラスが剥離した后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。実施例1ケン化度99.2モ
ル%、重合度1700のポリビニルアルコールの1鍾量
%水溶液100k9に濃塩酸(塩酸濃度35%)1kg
と過塩素酸ナトリウムの60%水溶液5k9とを加え(
過塩素ナトリウム濃度は最終系で4.2%)、1(3C
にて攪拌しつつブチルアルデヒ・ド5.1k9を滴下し
つつ3紛間加えたところ白色微粒子状のポリビニルブチ
ラールの沈澱が析出した。
The degree of exposure of the film after the glass was peeled off was determined using limit samples that had been graded in advance, and the results were expressed as pummel values according to Table 1. Example 1 1kg of concentrated hydrochloric acid (hydrochloric acid concentration 35%) was added to 100k9 of a 1% aqueous solution of polyvinyl alcohol with a degree of saponification of 99.2 mol% and a degree of polymerization of 1700.
and 5k9 of a 60% aqueous solution of sodium perchlorate (
The sodium perchlorate concentration in the final system was 4.2%), 1 (3C
When three powders of butyraldehyde 5.1k9 were added dropwise while stirring, white fine particles of polyvinyl butyral were precipitated.

さらに35%濃塩酸7k9を加え反応系を撹拌しつつ坐
℃/時間の昇温速度で35℃まで昇温し、更に帛時間そ
の温度を保つて熱成を行なつた後水酸化ナトリウムを加
えて反応系を中和しPHを9.6とした。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。
Further, 7k9 of 35% concentrated hydrochloric acid was added, and the reaction system was heated to 35°C at a heating rate of 8°C/hour while stirring, and the temperature was maintained for an additional time to perform thermal formation, and then sodium hydroxide was added. The reaction system was neutralized to a pH of 9.6. The obtained resin was washed with water and dried according to a conventional method to obtain a white fine powder.

このポリビニルブチラールのブチラール化度は62.0
%であつた。この様にして得られたポリビニルブチラー
ル、及び該ポリビニルブチラールに可塑剤としてトリエ
チレングリコールニジ2エチルブチレートを加えて得ら
れた中間膜、合せガラスの物性は第2表に示す通りであ
つた。
The degree of butyralization of this polyvinyl butyral is 62.0
It was %. The physical properties of the polyvinyl butyral thus obtained and the interlayer film and laminated glass obtained by adding triethylene glycol di-2-ethyl butyrate as a plasticizer to the polyvinyl butyral were as shown in Table 2.

実施例2 実施例1において、加えるブチルアルデヒドを5.2k
9とし、反応系を熱成温度40Cにて5時間維持した以
外はすべて実施例1と同様にして白色粉末を得た。
Example 2 In Example 1, the amount of butyraldehyde added was 5.2k.
A white powder was obtained in the same manner as in Example 1 except that the reaction system was maintained at a thermal formation temperature of 40 C for 5 hours.

この様にして得られたポリビニルブチラールのブチラー
ル化度は63.3モル%でありその物性等は第2表に示
す通りであつた。
The degree of butyralization of the polyvinyl butyral thus obtained was 63.3 mol %, and its physical properties were as shown in Table 2.

実施例3 実施例1において過塩素酸ナトリウム水溶液5kgの代
りに過塩素酸マグネシウム60%水溶液5kgを用い、
熱成温度を48℃、熱成時間を8時間とした以外はすべ
て実施例1と同様にして白色粉末を得た。
Example 3 In Example 1, 5 kg of 60% magnesium perchlorate aqueous solution was used instead of 5 kg of sodium perchlorate aqueous solution,
A white powder was obtained in the same manner as in Example 1 except that the thermal formation temperature was 48° C. and the thermal formation time was 8 hours.

この様にして得られたポリビニルブチラールのブチラー
ル化度は62.2モル%でありその物性等は第3表に示
す通りであつた。
The degree of butyralization of the polyvinyl butyral thus obtained was 62.2 mol%, and its physical properties were as shown in Table 3.

実施例4 ブチルアルデヒド5.5k9、過塩素酸ナトリウム60
%水溶液0.7kgを用い(最終系における濃度0.6
%)、熱成温度を60℃、熱成時間を3時間とした以外
はすべて実施例1と同様にして白色粉末を得た。
Example 4 Butyraldehyde 5.5k9, sodium perchlorate 60
% aqueous solution (concentration 0.6 in the final system)
%), a white powder was obtained in the same manner as in Example 1 except that the thermal formation temperature was 60° C. and the thermal formation time was 3 hours.

この様にして得られたポリビニルブチラールのブチラー
ル度は65.8モル%であり、その物性等は第4表に示
す通りであつた。実施例5 ブチルアルデヒド5.6kgを用い、熱成温度70等C
で反応系を3時間保つた以外はすべて実施例1と同様に
して白色粉末を得た。
The polyvinyl butyral thus obtained had a butyral degree of 65.8 mol%, and its physical properties were as shown in Table 4. Example 5 Using 5.6 kg of butyraldehyde, the thermal formation temperature was 70 C.
A white powder was obtained in the same manner as in Example 1 except that the reaction system was kept for 3 hours.

この様にして得られたポリビニルブチラールのブチラー
ル化度は67.7モル%であり、その特性等は第4表に
示す通りであつた。比較例1 実施例1において過塩素酸ナトリウムを加えない以外は
すべて実施例1と同様にしてポリビニルブチラールの粉
末を得た。
The polyvinyl butyral thus obtained had a degree of butyralization of 67.7 mol%, and its properties were as shown in Table 4. Comparative Example 1 Polyvinyl butyral powder was obtained in the same manner as in Example 1 except that sodium perchlorate was not added.

その物性等は第第5表に示す通りであつた。
ャ*比較例2) 実施例5において過
塩素酸ナトリウムを加えない以外はすべて実施例5と同
様にしてポリビニルブチラールの粉末を得た。
Its physical properties were as shown in Table 5.
*Comparative Example 2) Polyvinyl butyral powder was obtained in the same manner as in Example 5 except that sodium perchlorate was not added.

Claims (1)

【特許請求の範囲】 1 酸触媒の存在下に水相中でポリビニルアルコールと
ブチルアルデヒドを縮合せしめてポリビニルブチラール
を製造する方法において、反応系を20℃以下の温度に
保つて沈澱物を析出させたのち昇温し、過塩素酸系化合
物の存在下で、反応系を30℃以上の温度に保つて熱成
させることを特徴とするポリビニルブチラールの製造方
法。 2 最終反応系における過塩素酸系化合物の濃度が0.
2重量%以上である特許請求の範囲第1項記載の製造方
法。 3 過塩素酸系化合物が過塩素酸、過塩素酸のアルカリ
金属塩及び過塩素酸のアルカリ土類金属塩の内の少くと
も1つである特許請求の範囲第1項又は第2項記載の製
造方法。 4 過塩素酸のアルカリ金属塩が過塩素酸ナトリウムで
ある特許請求の範囲第3項記載の製造方法。 5 反応系を30℃以上の温度にて1〜15時間保つて
熱成させる特許請求の範囲第1項乃至第3項の何れかに
記載の製造方法。
[Claims] 1. A method for producing polyvinyl butyral by condensing polyvinyl alcohol and butyraldehyde in an aqueous phase in the presence of an acid catalyst, in which a precipitate is precipitated by maintaining the reaction system at a temperature of 20°C or less. A method for producing polyvinyl butyral, which comprises heating the reaction system and thermally forming the reaction system at a temperature of 30° C. or higher in the presence of a perchloric acid compound. 2 The concentration of perchloric acid compound in the final reaction system is 0.
The manufacturing method according to claim 1, wherein the content is 2% by weight or more. 3. Claim 1 or 2, wherein the perchloric acid compound is at least one of perchloric acid, an alkali metal salt of perchloric acid, and an alkaline earth metal salt of perchloric acid. Production method. 4. The manufacturing method according to claim 3, wherein the alkali metal salt of perchloric acid is sodium perchlorate. 5. The manufacturing method according to any one of claims 1 to 3, wherein the reaction system is maintained at a temperature of 30° C. or higher for 1 to 15 hours for thermal formation.
JP8305881A 1981-05-29 1981-05-29 Method for producing polyvinyl butyral Expired JPS6053042B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8305881A JPS6053042B2 (en) 1981-05-29 1981-05-29 Method for producing polyvinyl butyral

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8305881A JPS6053042B2 (en) 1981-05-29 1981-05-29 Method for producing polyvinyl butyral

Publications (2)

Publication Number Publication Date
JPS57195706A JPS57195706A (en) 1982-12-01
JPS6053042B2 true JPS6053042B2 (en) 1985-11-22

Family

ID=13791584

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8305881A Expired JPS6053042B2 (en) 1981-05-29 1981-05-29 Method for producing polyvinyl butyral

Country Status (1)

Country Link
JP (1) JPS6053042B2 (en)

Also Published As

Publication number Publication date
JPS57195706A (en) 1982-12-01

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