JPH0114922B2 - - Google Patents

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Publication number
JPH0114922B2
JPH0114922B2 JP15547481A JP15547481A JPH0114922B2 JP H0114922 B2 JPH0114922 B2 JP H0114922B2 JP 15547481 A JP15547481 A JP 15547481A JP 15547481 A JP15547481 A JP 15547481A JP H0114922 B2 JPH0114922 B2 JP H0114922B2
Authority
JP
Japan
Prior art keywords
polyvinyl butyral
temperature
manufacturing
weight
acid
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
JP15547481A
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Japanese (ja)
Other versions
JPS5857406A (en
Inventor
Kunio Yanagisawa
Takashi Nakagawa
Shigeru Nomura
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 JP15547481A priority Critical patent/JPS5857406A/en
Publication of JPS5857406A publication Critical patent/JPS5857406A/en
Publication of JPH0114922B2 publication Critical patent/JPH0114922B2/ja
Granted legal-status Critical Current

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Description

【発明の詳现な説明】[Detailed description of the invention]

本発明はポリビニルブチラヌルの補造方法に関
し、詳しくは、可塑剀を加えお合せガラス甚䞭間
膜を補造するず垞枩における䞭間膜同志の粘着性
以䞋䞭間膜の自着性ずいう。が倧巟に改善され
た合せガラス甚䞭間膜が埗られるポリビニルブチ
ラヌルの補造方法に関するものである。 今日、広く工業的に利甚されおいるポリビニル
ブチラヌルの補法は沈柱法ず溶解法ずに倧別され
る。この内沈柱法は、䟋えば、酞觊媒の存圚䞋で
ポリビニルアルコヌルの氎溶液にブチルアルデヒ
ドを加え20℃以䞋の比范的䜎枩床でブチラヌル化
反応を行いポリビニルブチラヌルの埮现沈柱を生
ぜしめた埌、曎に長時間撹拌、加熱する方法であ
る。又溶解法は、䟋えばむ゜プロピルアルコヌル
等の有機溶剀䞭にポリビニルアルコヌルを分散さ
せ酞觊媒の存圚䞋にブチルアルデヒドを加えお加
熱し長時間反応させる方法である。 然し乍ら、これら埓来の方法によ぀お補造され
たポリビニルブチラヌルに可塑剀を加えお埗られ
た合せガラス甚䞭間膜は、膜衚面の粘着性が匷い
為補膜埌の捲回時に膜同志が粘着するずいう問題
を有し、かかる粘着を防ぐ為に膜衚面に重炭酞゜
ヌダ等の粘着防止剀を散垃したり、20℃以䞋の枩
床に䞭間膜を冷华するこずが行なわれおいる。 しかし粘着防止剀を散垃する方法はポリビニル
ブチラヌル膜ずガラスずを接着する際に、事前に
粘着防止剀陀去の為の氎掗工皋及び也燥工皋を経
なければならないずいう難点を有し、たた冷凍法
は䞭間膜の補造から包装、茞送、保存そしお䜿甚
時たで冷凍装眮が必芁であり高䟡に぀くずいう難
点を有し、実質的に垞枩における自着性が無い䞭
間膜の出珟が埅たれおいた。 本発明はポリビニルブチラヌルの補造方法の䞊
述の珟状に鑑み、埗られたポリビニルブチラヌル
に可塑剀を加えお合せガラス甚䞭間膜を補造する
ず自着性が倧巟に改善された合せガラス甚䞭間膜
が埗られるポリビニルブチラヌルの補造方法を提
䟛するこずを目的ずするもので、その芁旚は、ポ
リビニルアルコヌルのアセタヌル化により埗られ
たポリビニルブチラヌルを氎盞䞭に分散させた状
態で、塩酞、臭化氎玠酞及び硝酞のそれぞれの氎
溶性塩の少くずも぀の存圚䞋に匷酞性領域で30
℃以䞊の枩床に保぀こずを特城ずする自着性が改
善されたポリビニルブチラヌルの補造方法に存す
る。 本発明に䟛されるポリビニルブチラヌルはポリ
ビニルアルコヌルのアセタヌル化により埗られた
ものであれば出発原料がポリビニルアセテヌトで
あ぀おもよく、可塑剀を加えるず自着性を有する
䞭間膜を圢成するものが広く䜿甚される。しかし
氎盞䞭に分散させるので、同様に氎盞䞭で補造し
たポリビニルブチラヌルを甚いるのが奜たしい。
この堎合に工業的に特に奜たしいのは、酞觊媒の
存圚䞋でポリビニルアルコヌルずブチルアルデヒ
ドずを反応させおポリビニルブチラヌルを氎盞䞭
で沈柱析出せしめた埌、該暹脂を反応系から分離
するこずなくそのたた同じ氎盞䞭で埌凊理するこ
ずである。しかし、䞊蚘沈柱法や溶解法等の埓来
公知の方法により埗られた也燥したポリビニルブ
チラヌル粉末の䜿甚も勿論可胜である。 本発明に甚いるポリビニルブチラヌルずしお
は、30℃以䞊の枩床に保぀お埗られたポリビニル
ブチラヌルを合せガラス甚䞭間膜ずしお甚いる堎
合はブチラヌル化床が60〜75モルであるこずが
望たしく、又、ケン化床が95モル以䞊、曎には
98モル以䞊のポリビニルアルコヌルから補せら
れたものであるのが、最終的に透明性の良奜な暹
脂が埗られる点で奜たしい。又このずきのポリビ
ニルアルコヌルの平均重合床は、䜎過ぎるず可塑
剀を加えお䞭間膜ずした堎合の自着性改善効果が
乏しく、高過ぎるず粘床が高くお工業的にアセタ
ヌル化するのに䞍郜合であるので、通垞は800〜
3000のものが甚いられる。 本発明における塩酞、臭化氎玠酞及び硝酞のそ
れぞれの氎溶性塩の奜適な䟋ずしおは、それぞれ
の陜性成分がマグネシりム、カルシりム、亜鉛、
アルミニりム、鉄、チタン等の䟡以䞊の原子䟡
を有するものが挙げられる。これらの塩はそれぞ
れ単独で又は適宜組合わせお甚いられ、その䜿甚
量は通垞分散させたポリビニルブチラヌル100重
量郚に察しお〜100重量郚奜たしくは〜30重
量郚、ずされる。 本発明におけるポリビニルブチラヌルの分散液
濃床は暹脂が氎盞䞭に分散される濃床であれば特
に限定されないが、通垞〜15重量ずされる。
この時埮量のアルデヒドが䞊蚘分散液䞭に存圚し
おいおもよく、その量は通垞分散液の重量以
䞋ずされる。 䞊蚘氎溶性塩のポリビニルブチラヌル分散液ぞ
の添加は、ポリビニルアルコヌルのアセタヌル化
埌に高枩で䜙り長時間を経過しない内に行うの
が、ポリビニルブチラヌル粒子の粗倧化を防止す
る䞊で奜たしい。 本発明においお匷酞性領域のポリビニルブチラ
ヌル分散液を埗るには、埓来公知の塩酞、硫酞、
硝酞等の無機酞やパラトル゚ンスルホン酞等の有
機酞を甚いお埗られた匷酞性氎盞䞭に也燥したポ
リビニルブチラヌルを加えおもよく、前蚘ポリビ
ニルブチラヌルを氎盞に分散しおからのちに前蚘
酞を加えおもよく、或いは又匷酞性氎盞䞭にポリ
ビニルブチラヌルを沈柱析出せしめおもよい。 本発明における匷酞性領域ずは、ポリビニルブ
チラヌル分散液の枩床にもよるが通垞PH以䞋ず
され、奜たしくはPH以䞋ずされる。又、ポリビ
ニルブチラヌルのブチラヌル化床を増倧させる必
芁のある堎合は、前蚘分散液䞭に所定量のブチル
アルデヒドを存圚せしめるこずにより、ブチラヌ
ル化の増倧を行うこずが出来る。 又、ポリビニルブチラヌルの熟成の枩床の䞊限
は特に定められないが䞀般に90℃以䞋ずされ、30
℃以䞊の枩床に保぀時間は、分散液の昇枩及び降
枩の時間を含め通垞は〜20時間ずされる。 本発明方法によりポリビニルブチラヌルを補造
するには、通垞は、20℃を越える枩床のポリビニ
ルアルコヌル氎溶液に酞觊媒を加え、次いで反応
系を冷华し、ブチルアルデヒドを加えお瞮合反応
させおポリビニルブチラヌルの沈柱を20℃以䞋の
劂く䜎枩で析出せしめお、氎盞䞭に分散させたポ
リビニルブチラヌルを甚意する。 この様に沈柱析出時に反応系の枩床を䜎く保぀
のは沈柱物を埮小な粒子状又は粉状で埗るためで
あり、枩床の䞋限は、反応系が凍結しない様な枩
床であればよく特に制限されるものではないが、
通垞−℃以䞊の枩床が採甚される。 次に反応系のPHが以䞋の状態で䞊蚘塩の少く
ずも぀を加え反応系を昇枩し30℃以䞊の枩床に
保぀お反応を曎に進行せしめた埌、觊媒を塩基で
䞭和し、反応生成物を取り出しお垞法により掗
浄、粟補を行うのである。 この様に、ポリビニルアルコヌルのアセタヌル
化により埗られたポリビニルブチラヌルを氎盞䞭
に分散させた状態で、塩酞、臭化氎玠酞及び硝酞
の倫々の氎溶性塩の少くずも぀の存圚䞋に匷酞
性領域で前蚘分散液の枩床を30℃以䞊に保぀こず
により、可塑剀を加えお合せガラス甚䞭間膜を補
造するず実質的に垞枩における自着性がない䞭間
膜が埗られるのであり、この様に自着性が改善さ
れたポリビニルブチラヌルが補造される理由に぀
いおは未だ充分には明らかではないが、次の通り
掚枬される。 ブチラヌル化反応は平衡反応であるので、反応
が或る皋床進行した平衡状態においお、ブチラヌ
ル化床はほが䞀定ずなる。埓来公知の補造方法で
は䞀般に、ブチラヌル化床が䞀定の状態に達する
前に反応を停止しおいたのであり、この時のポリ
ビニルブチラヌル䞭の残氎酞基はランダムな配列
をしおいるず考えられる。しかしおこのポリビニ
ルブチラヌルを氎盞䞭に分散させ、䞊蚘塩の存圚
䞋に匷酞性領域で前蚘分散液の枩床を30℃以䞊に
保぀ず、匷酞性領域䞋で生じる逆ブチラヌル化反
応により生成する氎酞基は氎玠結合による䌚合を
瀺す傟向があり、䞀方ブチラヌル化反応は、䌚合
の傟向の匷い氎酞基よりもそうでない氎酞基に遞
択的に起り易くなる。埓぀お最終的平衡状態に近
ずくず、分子内に氎酞基が連鎖的に残る傟向が匷
たり、これによ぀お埗られたポリビニルブチラヌ
ルの剛性が増加し、これが䞭間膜ずしお甚いられ
た際の自着性の枛少すなわち改善に寄䞎するもの
ず考えられる。 本発明者等は、䞊蚘塩の䞍存圚䞋でもポリビニ
ルブチラヌルの分散液を匷酞性域で比范的高枩で
長時間保぀たポリビニルブチラヌルに可塑剀を加
えるず自着性が改善された䞭間膜が埗られるずい
う知芋をすでに埗たものであるが、本発明におけ
る䞊蚘塩を䜿甚するず䞊蚘枩床及び時間の条件が
著しく緩和され工皋䞊有利になるのである。 又、䟋えば沈柱法においおポリビニルブチラヌ
ルの埮现粒子を析出せしめた埌、䞊蚘塩の䞍存圚
䞋では高枩で長時間保぀ず沈柱粒子の凝集等によ
る粗倧化が生じ易くなり、粗倧化した粒子䞭には
酞觊媒やその䞭和に甚いた塩基等が残溜しお透明
性曎には熱安定性を䜎䞋せしせる傟向があ぀た
が、䞊蚘塩には埮粒子の粗倧化を防止する䜜甚が
あり透明性や熱安定性を䜎䞋せしめるこずが殆ん
どないのである。 本発明方法により埗られたポリビニルブチラヌ
ルに甚いる可塑剀は埓来よりポリビニルブチラヌ
ルの為の可塑剀ずしお甚いられるものをいずれも
䜿甚するこずができ、䟋えばトリ゚チレングリコ
ヌルゞ゚チルブチレヌト、トリ゚チレングリ
コヌルゞ゚チルヘキ゜゚ヌトなどの汎甚可塑
剀が挙げられる。曎にゞブトキシゞ゚チレングリ
コヌルアゞペヌトなどが奜適に䜿甚される。可塑
剀の添加量はポリビニルブチラヌル100重量郚に
察し、30乃至60重量郚が望たしい。可塑剀が30重
量郚未満では合せガラス甚䞭間膜ずした時の耐貫
通性が䜎䞋し、可塑剀が60重量郚を越えるものは
可塑剀が膜衚面にしみ出すいわゆるブリヌド珟象
が生じ、合わせガラス甚䞭間膜ずした時の透明性
及び接着性に悪圱響を及がすからである。 本発明方法は䞊述の通りの構成になされおお
り、本発明によれば、可塑剀を加えお合せガラス
甚䞭間膜を補造するず垞枩における自着性が顕著
に改善された合せガラス甚䞭間膜が埗られるポリ
ビニルブチラヌルが塩酞、臭化氎玠酞及び硝酞の
それぞれの氎溶性塩の䜕れをも甚いない堎合に比
范しお工業的に有利な枩床・時間の条件䞋で埗る
こずができるのである。 又、本発明においお埮现なポリビニルブチラヌ
ル粒子を甚いた堎合は、粗倧化粒子が殆んど残溜
しおいない透明性、熱安定性の良奜なポリビニル
ブチラヌルを埗るこずができるのである。 以䞋に本発明の実斜䟋を瀺す。単にずあるの
は重量を意味する。尚、実斜䟋における各物性
倀は次の枬定法によ぀た。  透明性 ポリビニルブチラヌルが二枚のガラス板の間
に挟んで埗られた詊料を加熱されたオヌブン䞭
に入れおポリビニルブチラヌルを溶融した埌に
宀枩で攟冷した。埗られた詊料を癜色光のもず
で芳察し、青味、濁り等のないものを良奜ずし
た。  熱安定性 ポリビニルブチラヌルを入れた詊隓管を加枩
された油济に浞し、120℃にお所定時間を経お
もポリビニルブチラヌルが倉色しない堎合を熱
安定性が良奜であるずした。 䞀般に䞭和又は氎掗が䞍完党な堎合にはポリ
ビニルブチラヌル䞭に塩酞等の觊媒が残存し、
本詊隓を行うずポリビニルブチラヌルは黄色に
着色する。  自着性 ポリビニルブチラヌル100重量郚に所定の可
塑剀42重量郚を加えラむカむ機で15分間混合
し、ロヌルを甚い120℃にお分間混緎した埌
150℃、40Kgcm2にお分間プレスし衚面の平
滑な厚さ0.76mmの均䞀なフむルムを䜜成した。
このフむルムをcm×10cmの長方圢状に切り取
り、枚重ね合わせKgの荷重をかけた状態で
20℃の枩床に保぀たデシケヌタヌ䞭にお48時間
攟眮した。 この様にしお埗られた詊料の䞀端を互に剥
し、剥されたフむルムを90℃方向に曲げお党䜓
を字圢にした埌、剥されたフむルムの䞡方の
端を匕匵詊隓機で぀かみ20℃にお500mm分の
匕匵速床で型剥離匷床を枬定した。  耐衝撃性 ポリビニルブチラヌル100重量郚に可塑剀42
重量郚を添加混緎し、抌し出し機にお、厚さ
0.76mmの可塑化ポリビニルブチラヌルを埗た。
このフむルムを厚さ3.0mm、30cm×30cmのガラ
ス板板の間に挟み蟌み、埓来公知の条件で加
熱加圧しお合わせガラスを埗た。この合せガラ
スを所定枩床に時間以䞊保管した埌、倖枠が
31cm×31cm、内枠が26cm×26cm、高さ20cmのマ
ス型鉄枠䞊に氎平に眮き、2.268Kgポンド
の鋌球を指定された高さから合わせガラスの䞭
心に萜䞋させた。 合せガラスを鋌球が貫通する割合が50ずな
る高さを耐貫通匷床ずした。 尚、合せガラスの詊料ずしおは、予め金属石
けんを適宜添加混合した可塑剀を甚いるこずに
より埌述するバンメル倀を補品ずしお通垞䜿甚
される範囲のに蚭定したものを甚いた。  ガラスに察する接着性 合せガラスを−18℃±0.6℃の枩床に16時間
攟眮しお調敎し、これを頭郚が0.45Kgのハンマ
ヌで打぀おガラスの粒埄がmm以䞋になる迄粉
砕した。ガラスが剥離した后の膜の露出床をあ
らかじめグレヌド付けした限床芋本で刀定し、
その結果を第衚に埓いバンメル倀ずしお衚わ
した。
The present invention relates to a method for producing polyvinyl butyral, and more specifically, when an interlayer film for laminated glass is produced by adding a plasticizer, the adhesion of the interlayer films to each other at room temperature (hereinafter referred to as self-adhesion of the interlayer film) is greatly improved. The present invention relates to a method for producing polyvinyl butyral that yields a polyvinyl butyral interlayer film for laminated glass. The methods for producing polyvinyl butyral that are widely used industrially today are broadly divided into precipitation methods and dissolution methods. In this internal precipitation method, for example, butyraldehyde is added to an aqueous solution of polyvinyl alcohol in the presence of an acid catalyst, a butyralization reaction is carried out at a relatively low temperature of 20°C or less to produce fine precipitates of polyvinyl butyral, and then the precipitation is further continued. This method involves stirring and heating for a period of time. The dissolution method is, for example, a method in which polyvinyl alcohol is dispersed in an organic solvent such as isopropyl alcohol, and butyraldehyde is added in the presence of an acid catalyst, and the mixture is heated and reacted for a long time. However, interlayer films for laminated glass obtained by adding plasticizers to polyvinyl butyral produced by these conventional methods have strong adhesion on the film surface, so the films tend to stick to each other during winding after film formation. In order to prevent such adhesion, methods include spraying an anti-adhesive agent such as sodium bicarbonate on the surface of the film or cooling the interlayer film to a temperature of 20° C. or lower. However, 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 problem is that a refrigeration device is required for the production, packaging, transportation, storage, and use of the interlayer film, which is expensive, and the emergence of an interlayer film that is substantially free of self-adhesion at room temperature has been awaited. In view of the above-mentioned current state of the method for producing polyvinyl butyral, the present invention provides an interlayer film for laminated glass with greatly improved self-adhesion by adding a plasticizer to the obtained polyvinyl butyral to produce an interlayer film for laminated glass. The purpose is to provide a method for producing polyvinyl butyral obtained by acetalizing polyvinyl alcohol, and the gist thereof is to disperse hydrochloric acid, hydrobromic acid, 30 in the strongly acidic region in the presence of at least one respective water-soluble salt of nitric acid and nitric acid.
The present invention provides a method for producing polyvinyl butyral with improved self-adhesiveness, characterized by maintaining the temperature at a temperature of 0.degree. C. or higher. The polyvinyl butyral used in the present invention may be polyvinyl acetate as a starting material as long as it is obtained by acetalizing polyvinyl alcohol. Widely used. However, since it is dispersed in the aqueous phase, it is preferred to use polyvinyl butyral which is also produced in the aqueous 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 butyral in the aqueous phase, without separating the resin from the reaction system. This means post-treatment in the same aqueous phase. However, it is of course possible to use dried polyvinyl butyral powder obtained by conventionally known methods such as the above-mentioned precipitation method or dissolution method. As for the polyvinyl butyral used in the present invention, when polyvinyl butyral obtained by keeping the temperature at 30°C or higher is used as an interlayer film for laminated glass, it is desirable that the degree of butyralization is 60 to 75 mol%. The degree of oxidation is 95 mol% or more, and
It is preferable that the resin be made from polyvinyl alcohol containing 98 mol% or more, since a resin with good transparency can be obtained in the end. In addition, if the average degree of polymerization of polyvinyl alcohol at this time is too low, the effect of improving self-adhesion when forming an interlayer film by adding a plasticizer is poor, and if it is too high, the viscosity is high, which is inconvenient for industrial acetalization. Therefore, it is usually 800~
3000 are used. Preferred examples of water-soluble salts of hydrochloric acid, hydrobromic acid and nitric acid in the present invention include magnesium, calcium, zinc,
Examples include those having a valence of two or more, such as aluminum, iron, and titanium. These salts may be used alone or in appropriate combinations, and the amount used is usually 2 to 100 parts by weight, preferably 5 to 30 parts by weight, per 100 parts by weight of the dispersed polyvinyl butyral. The concentration of the polyvinyl butyral dispersion in the present invention is not particularly limited as long as the resin is dispersed in the aqueous phase, but it is usually 3 to 15% by weight.
At this time, a trace amount of aldehyde may be present in the dispersion, and the amount thereof is usually 1% by weight or less of the dispersion. In order to prevent the polyvinyl butyral particles from becoming coarse, it is preferable to add the water-soluble salt to the polyvinyl butyral dispersion before a too long period of time has elapsed at a high temperature after polyvinyl alcohol is acetalized. In the present invention, in order to obtain a polyvinyl butyral dispersion in a strongly acidic region, conventionally known hydrochloric acid, sulfuric acid,
Dry polyvinyl butyral may be added to a strongly acidic aqueous phase obtained using an inorganic acid such as nitric acid or an organic acid such as para-toluenesulfonic acid, and after dispersing the polyvinyl butyral in the aqueous phase, An acid may be added or the polyvinyl butyral may be precipitated in a strongly acidic aqueous phase. The strongly acidic region in the present invention is usually PH2 or less, preferably PH1 or less, although it depends on the temperature of the polyvinyl butyral dispersion. Furthermore, when it is necessary to increase the degree of butyralization of polyvinyl butyral, the degree of butyralization can be increased by making a predetermined amount of butyraldehyde exist in the dispersion. In addition, the upper limit of the temperature for ripening polyvinyl butyral is not particularly set, but it is generally set at 90°C or lower, and 30°C or lower.
The time for maintaining the temperature at or above .degree. C. is usually 1 to 20 hours, including the time for raising and lowering the temperature of the dispersion. To produce polyvinyl butyral by the method of the present invention, usually an acid catalyst is added to an aqueous polyvinyl alcohol solution at a temperature exceeding 20°C, the reaction system is then cooled, and butyraldehyde is added to cause a condensation reaction to precipitate polyvinyl butyral. Polyvinyl butyral is prepared by precipitating it at a low temperature such as 20°C or lower and dispersing it in an aqueous phase. In this way, the temperature of the reaction system is kept low during precipitation in order to obtain the precipitate in the form of fine particles or powder, and the lower limit of the temperature should be a temperature that does not freeze the reaction system, and there are no particular restrictions. Although it is not something that will be done,
Usually a temperature of -6°C or higher is employed. Next, while the pH of the reaction system is 2 or less, at least one of the above salts is added and the reaction system is heated and kept at a temperature of 30°C or higher to further advance the reaction, and then the catalyst is neutralized with a base. Then, the reaction product is taken out and washed and purified using conventional methods. In this way, polyvinyl butyral obtained by acetalization of polyvinyl alcohol is dispersed in an aqueous phase, and then a strong acid is added to the polyvinyl butyral in the presence of at least one water-soluble salt of hydrochloric acid, hydrobromic acid, and nitric acid. If an interlayer film for laminated glass is manufactured by adding a plasticizer by maintaining the temperature of the dispersion liquid at 30°C or higher in the temperature range, an interlayer film that has virtually no self-adhesion at room temperature can be obtained. The reason why polyvinyl butyral with improved self-adhesiveness is produced is not yet fully clear, but it is speculated as follows. Since the butyralization reaction is an equilibrium reaction, the degree of butyralization becomes approximately constant in an equilibrium state where the reaction has progressed to a certain extent. In conventional production methods, the reaction was generally stopped before the degree of butyralization reached a certain level, and the remaining hydroxyl groups in the polyvinyl butyral at this time are thought to be randomly arranged. However, when this polyvinyl butyral is dispersed in an aqueous phase and the temperature of the dispersion is maintained at 30°C or higher in a strongly acidic region in the presence of the above salt, hydroxyl groups are generated by the reverse butyralization reaction that occurs in a strongly acidic region. tends to exhibit association by hydrogen bonding, while the butyralization reaction is more likely to occur selectively with hydroxyl groups that do not have a strong tendency to associate than with hydroxyl groups that have a strong tendency to associate. Therefore, as the final equilibrium state approaches, the tendency for hydroxyl groups to remain in a chain within the molecule increases, which increases the rigidity of the resulting polyvinyl butyral, which leads to self-adhesion when used as an interlayer film. It is thought that this contributes to the reduction, or improvement, of sexual performance. The present inventors have found that by keeping a dispersion of polyvinyl butyral in a strongly acidic region at a relatively high temperature for a long period of time, and adding a plasticizer to the polyvinyl butyral, even in the absence of the above salt, an interlayer film with improved self-adhesion was obtained. However, when the above-mentioned salt is used in the present invention, the above-mentioned temperature and time conditions are significantly relaxed, which is advantageous in the process. In addition, for example, after fine particles of polyvinyl butyral are precipitated by a precipitation method, if they are kept at high temperature for a long time in the absence of the above salt, coarsening due to agglomeration of the precipitated particles is likely to occur, and some of the coarse particles are The acid catalyst and the base used to neutralize it tended to remain, reducing transparency and thermal stability; however, the above-mentioned salt has the effect of preventing fine particles from becoming coarse, and thus improving transparency. There is almost no reduction in thermal stability. As the plasticizer used for the polyvinyl butyral obtained by the method of the present invention, any of those conventionally used as a plasticizer for polyvinyl butyral can be used, such as triethylene glycol di2-ethyl butyrate, triethylene glycol Examples include general-purpose plasticizers such as di-2-ethylhexoate. Furthermore, dibutoxydiethylene glycol adipate and the like are preferably used. The amount of plasticizer added is preferably 30 to 60 parts by weight per 100 parts by weight of polyvinyl butyral. If the plasticizer content is less than 30 parts by weight, the penetration resistance will decrease when used as an interlayer film for laminated glass, and if the plasticizer content exceeds 60 parts by weight, a so-called bleed phenomenon will occur in which the plasticizer seeps onto the film surface, resulting in poor performance of laminated glass. This is because it has an adverse effect on transparency and adhesion when used as an interlayer film. The method of the present invention is configured as described above, and according to the present invention, when an interlayer film for laminated glass is manufactured by adding a plasticizer, an interlayer film for laminated glass with significantly improved self-adhesion at room temperature can be obtained. The resulting polyvinyl butyral can be obtained under industrially advantageous temperature and time conditions compared to the case where none of the water-soluble salts of hydrochloric acid, hydrobromic acid and nitric acid are used. Furthermore, when fine polyvinyl butyral particles are used in the present invention, it is possible to obtain polyvinyl butyral with good transparency and thermal stability in which almost no coarse particles remain. Examples of the present invention are shown below. % simply means weight %. In addition, each physical property value in Examples was based on the following measuring method. 1 Transparency A sample obtained by sandwiching polyvinyl butyral between two glass plates was placed in a heated oven to melt the polyvinyl butyral, and then 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. Thermal stability A test tube containing polyvinyl butyral was immersed in a heated oil bath, and the thermal stability was determined to be good if the polyvinyl butyral did not change color even after a predetermined period of time at 120°C. Generally, when neutralization or water washing is incomplete, catalysts such as hydrochloric acid remain in polyvinyl butyral.
When this test is performed, polyvinyl butyral is colored yellow. 3 Self-adhesiveness Add 42 parts by weight of the specified plasticizer to 100 parts by weight of polyvinyl butyral, mix for 15 minutes using a Laikai machine, and knead for 3 minutes at 120°C using a roll.
A uniform film with a smooth surface and a thickness of 0.76 mm was prepared by pressing at 150° C. and 40 kg/cm 2 for 3 minutes.
Cut this film into a rectangular shape of 3cm x 10cm, stack the two pieces together and apply a load of 6kg.
It was left for 48 hours in a desiccator kept at a temperature of 20°C. One end of the sample obtained in this way was peeled off from each other, and the peeled film was bent in a direction of 90°C to form a T-shape, and then both ends of the peeled film were held in a tensile tester and heated to 20°C. The T-peel strength was measured at a tensile speed of 500 mm/min. 4 Impact resistance 100 parts by weight of polyvinyl butyral and 42 parts by weight of plasticizer
Add and knead parts by weight, and use an extruder to measure the thickness.
0.76 mm of plasticized polyvinyl butyral was obtained.
This film was sandwiched between two glass plates of 3.0 mm thickness and 30 cm x 30 cm, and heated and pressed under conventionally known conditions to obtain a laminated glass. After storing this laminated glass at the specified temperature for more than 8 hours, the outer frame
Placed horizontally on a square iron frame with a size of 31cm x 31cm, an inner frame of 26cm x 26cm, and a height of 20cm, weighing 2.268Kg (5 pounds).
A steel ball was dropped from a specified height onto the center of the laminated glass. The height at which 50% of the steel balls penetrate the laminated glass is defined as the penetration resistance. The laminated glass sample used was one in which the Bummel 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. 5. Adhesion to glass The laminated glass was adjusted by leaving it at a temperature of -18°C ± 0.6°C for 16 hours, and was crushed by hitting it with a hammer with a head weighing 0.45 kg until the particle size of the glass became 6 mm or less. After the glass has peeled off, the degree of exposure of the film is determined using pre-graded limit samples.
The results were expressed as Bummel values according to Table 1.

【衚】 実斜䟋  ケン化床99.6モル、重合床2100のポリビニル
アルコヌルの13氎溶液100Kgに濃塩酞濃床35
Kgを加え、13℃にお撹拌し぀぀30分間芁し
おブチルアルデヒド6.7Kgを滎䞋したずころ癜色
埮粒子状のポリビニルブチラヌルの沈柱が析出し
た。さらに35濃塩酞Kgを加えお撹拌し反応系
のPHを0.5以䞋にし、臭化カルシりムの16氎溶
液15.3Kgを加え臭化カルシりムの量は最終的に
埗られたポリビニルブチラヌル100重量郚に察し
お20重量郚であ぀た。20℃時間の昇枩速床で
40℃たで昇枩し、曎に時間その枩床を保぀お熟
成を行な぀た埌氎酞化ナトリりムを加えお反応系
を䞭和しPHを9.6ずした。30℃以䞊の枩床に保぀
た時間は6.8時間であ぀た。 埗られた暹脂を垞法に埓い氎掗、也燥を行ない
癜色埮粉末を埗た。このポリビニルブチラヌルの
ブチラヌル化床は66.4であ぀た。 この様にしお埗られたポリビニルブチラヌル、
該ポリビニルブチラヌル10Kgに可塑剀ずしおトリ
゚チレングリコヌルゞ゚チルブチレヌト4.2
Kgを加えお埗られた䞭間膜及び該䞭間膜から埗ら
れた合せガラスの物性は第衚に瀺す通りであ぀
た。 実斜䟋  実斜䟋においお臭化カルシりムの代りに塩化
第二鉄を甚いた以倖は党お実斜䟋ず同様にしお
ポリビニルブチラヌルの粉末を埗た。その物性等
は第衚に瀺す通りであ぀た。 実斜䟋  実斜䟋ず同様にしお反応系䞭に癜色埮粒子状
のポリビニルブチラヌルの沈柱を析出せしめた。
さらに臭化カルシりムの代りに臭化マグネシりム
を加えたのち60℃に昇枩しおその枩床に時間保
぀た以倖は実斜䟋ず同様にしおポリビニルブチ
ラヌルの粉末を埗た。その物性等は第衚に瀺す
通りであ぀た。 実斜䟋  実斜䟋においお臭化カルシりムの代りに硝酞
亜鉛を甚いた以倖は党お実斜䟋ず同様にしおポ
リビニルブチラヌルの粉末を埗た。その物性は第
衚に瀺す通りであ぀た。 実斜䟋  ケン化床99.6モル、重合床2100のポリビニル
アルコヌルの13氎溶液100Kgに濃塩酞濃床35
Kgを加え13℃にお撹拌し぀぀ブチルアルデ
ヒド6.7Kgを30分間芁しお加えたずころ癜色埮粒
子状のポリビニルブチラヌルの沈柱が埗られた。
さらに濃塩酞Kgを加え反応系を撹拌し぀぀20
℃時間の昇枩速床で40℃たで昇枩しおその枩
床に時間保぀た埌、垞法により䞭和、氎掗工皋
を経おブチラヌル化床65.8モル、平均粒埄175ÎŒ
の也燥したポリビニルブチラヌルを埗た。 臭化亜鉛の12氎溶液8.4Kgに濃床35の塩酞
Kgを加え䞊蚘也燥ポリビニルブチラヌル10Kgを
分散させ分散液のPHは0.5以䞋であ぀た。、該
分散液を48℃にお時間保぀た埌、氎酞化ナトリ
りムを加えお䞭和しPHを8.6ずし以䞋実斜䟋ず
同様にしおポリビニルブチラヌルの粉末を埗た。
その物性等は第衚に瀺す通りであ぀た。 比范䟋  実斜䟋においお臭化カルシりムを加えない以
倖はすでお実斜䟋ず同様にしおポリビニルブチ
ラヌルの粉末を埗た。その物性等は第衚に瀺す
通りであ぀た。 比范䟋  実斜䟋においお臭化マグネシりムを加えない
以倖はすべお実斜䟋ず同様にしおポリビニルブ
チラヌルの粉末を埗た。その物性等は第衚に瀺
す通りであ぀た。 比范䟋  実斜䟋においお臭化亜鉛を甚いない以倖はす
べお実斜䟋ず同様にしお埌段のポリビニルブチ
ラヌルの粉末を埗た。その物性等は第衚瀺す通
りであ぀た。
[Table] Example 1 Concentrated hydrochloric acid (concentration 35
%) was added thereto, and 6.7 kg of butyraldehyde was added dropwise over 30 minutes while stirring at 13°C, resulting in the precipitation of white fine particles of polyvinyl butyral. Furthermore, 7 kg of 35% concentrated hydrochloric acid was added and stirred to bring the pH of the reaction system below 0.5, and 15.3 kg of a 16% aqueous solution of calcium bromide was added (the amount of calcium bromide was determined based on 100 parts by weight of the final polyvinyl butyral). (20 parts by weight) at a heating rate of 20°C/hour.
The temperature was raised to 40°C and the temperature was maintained for an additional 6 hours for ripening, and then sodium hydroxide was added to neutralize the reaction system and the pH was adjusted to 9.6. The time that the temperature was maintained at 30°C or higher was 6.8 hours. The obtained resin was washed with water and dried according to a conventional method to obtain a white fine powder. The degree of butyralization of this polyvinyl butyral was 66.4%. Polyvinyl butyral obtained in this way,
Triethylene glycol = di-2-ethyl butyrate 4.2 as a plasticizer to 10 kg of the polyvinyl butyral.
The physical properties of the interlayer film obtained by adding Kg and the laminated glass obtained from the interlayer film were as shown in Table 2. Example 2 Polyvinyl butyral powder was obtained in the same manner as in Example 1 except that ferric chloride was used instead of calcium bromide. Its physical properties were as shown in Table 2. Example 3 In the same manner as in Example 1, fine white particles of polyvinyl butyral were precipitated in the reaction system.
Further, polyvinyl butyral powder was obtained in the same manner as in Example 1, except that magnesium bromide was added instead of calcium bromide, the temperature was raised to 60°C, and the temperature was maintained for 3 hours. Its physical properties were as shown in Table 2. Example 4 Polyvinyl butyral powder was obtained in the same manner as in Example 1 except that zinc nitrate was used instead of calcium bromide. Its physical properties were as shown in Table 2. Example 5 Concentrated hydrochloric acid (concentration 35
%) and 6.7 kg of butyraldehyde was added over a period of 30 minutes while stirring at 13°C, resulting in the precipitation of white fine particles of polyvinyl butyral.
Add 7 kg of concentrated hydrochloric acid and stir the reaction system for 20 minutes.
After increasing the temperature to 40℃ at a heating rate of ℃/1 hour and keeping it at that temperature for 3 hours, it was neutralized and washed with water using a conventional method to obtain a butyralization degree of 65.8 mol% and an average particle size of 175ÎŒ.
dry polyvinyl butyral was obtained. 6 kg of 35% hydrochloric acid was added to 8.4 kg of a 12% aqueous solution of zinc bromide to disperse 10 kg of the above dry polyvinyl butyral (PH of the dispersion was 0.5 or less), and the dispersion was heated at 48°C for 5 hours. After the mixture was maintained, sodium hydroxide was added to neutralize it to a pH of 8.6, and the same procedure as in Example 1 was carried out to obtain polyvinyl butyral powder.
Its physical properties were as shown in Table 2. Comparative Example 1 Polyvinyl butyral powder was obtained in the same manner as in Example 1 except that calcium bromide was not added. Its physical properties were as shown in Table 2. Comparative Example 2 Polyvinyl butyral 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 Table 2. Comparative Example 3 A polyvinyl butyral 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 were as shown in the second display.

【衚】【table】

【衚】 ※ 金属石けんを䞭間膜に含有ささお予めパンメ
ル倀がになる様に蚭定したガラスをサ
ンプルずしお甚いた。
[Table] * Glass containing metallic soap in the interlayer film and having a pummel value of 6 was used as a sample.

Claims (1)

【特蚱請求の範囲】  ポリビニルアルコヌルのアセタヌル化により
埗られたポリビニルブチラヌルを氎盞䞭に分散さ
せた状態で、塩酞、臭化氎玠酞及び硝酞のそれぞ
れの氎溶性塩の少くずも぀の存圚䞋に匷酞性領
域で30℃以䞊の枩床に保぀こずを特城ずする自着
性が改善されたポリビニルブチラヌルの補造方
法。  氎溶性塩の量が分散液䞭のポリビニルブチラ
ヌル100重量郚に察しお重量郚以䞊である第
項蚘茉の補造方法。  氎溶性塩の陜性成分がマグネシりム、カルシ
りム、亜鉛、アルミニりム、鉄、チタンのうちの
少くずも぀である第項又は第項蚘茉の補造
方法。  35℃以䞊の枩床に保぀時間が〜20時間であ
る第項〜第項䜕れか項に蚘茉の補造方法。  匷酞性領域のPHが以䞊である第項〜第
項䜕れか項に蚘茉の補造方法。  アセタヌル化により埗られたポリビニルブチ
ラヌルを、反応系から分離するこずなく同じ氎盞
䞭で熟成する第項〜第項䜕れか項に蚘茉の
補造方法。
[Scope of Claims] 1. Polyvinyl butyral obtained by acetalization of polyvinyl alcohol is dispersed in an aqueous phase in the presence of at least one water-soluble salt of hydrochloric acid, hydrobromic acid, and nitric acid. A method for producing polyvinyl butyral with improved self-adhesion, which comprises maintaining the polyvinyl butyral at a temperature of 30°C or higher in a strongly acidic region. 2 The first type in which the amount of water-soluble salt is 2 parts by weight or more based on 100 parts by weight of polyvinyl butyral in the dispersion.
Manufacturing method described in section. 3. The manufacturing method according to item 1 or 2, wherein the positive component of the water-soluble salt is at least one of magnesium, calcium, zinc, aluminum, iron, and titanium. 4. The manufacturing method according to any one of Items 1 to 3, wherein the time for maintaining the temperature at 35°C or higher is 1 to 20 hours. 5 Items 1 to 4 where the pH in the strongly acidic region is 2 or more
1. The manufacturing method according to any one of the above. 6. The manufacturing method according to any one of Items 1 to 5, wherein the polyvinyl butyral obtained by acetalization is aged in the same aqueous phase without being separated from the reaction system.
JP15547481A 1981-09-29 1981-09-29 Production of polyvinyl butyral having improved autohesion Granted JPS5857406A (en)

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 JPS5857406A (en) 1983-04-05
JPH0114922B2 true 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)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6483024A (en) * 1987-09-25 1989-03-28 Kyukyu Yakuhin Kogyo Kk Cataplasm for cold
CN100575368C (en) * 2004-08-04 2009-12-30 积氎化孊工䞚株匏䌚瀟 The manufacture method of the manufacture method of polyvinyl acetal resin, polyvinyl butyral resin and esterified polyvinyl alcohol resin

Also Published As

Publication number Publication date
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