JPH07206484A - Production of intermediate film for laminated glass - Google Patents

Production of intermediate film for laminated glass

Info

Publication number
JPH07206484A
JPH07206484A JP6152030A JP15203094A JPH07206484A JP H07206484 A JPH07206484 A JP H07206484A JP 6152030 A JP6152030 A JP 6152030A JP 15203094 A JP15203094 A JP 15203094A JP H07206484 A JPH07206484 A JP H07206484A
Authority
JP
Japan
Prior art keywords
extruder
raw material
laminated glass
group
coupling agent
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.)
Pending
Application number
JP6152030A
Other languages
Japanese (ja)
Inventor
Yasuto Jiyuni
康人 潤井
Satoshi Hayashi
聡史 林
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 JP6152030A priority Critical patent/JPH07206484A/en
Publication of JPH07206484A publication Critical patent/JPH07206484A/en
Pending legal-status Critical Current

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  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Joining Of Glass To Other Materials (AREA)

Abstract

PURPOSE:To obtain the intermediate film which has been kneaded and extrusion- molded in the same stage by extrusion-molding an ethylene-vinyl acetate copolymer, the condensation product of >=5-valency alcohol and benzaldehyde and a silane coupling agent under specified conditions. CONSTITUTION:An ethylene-vinyl acetate copolymer, the condensation product of the >=5-valency alcohol and benzaldehyde and a silane coupling agent having >=1 kind of group from among the amino group, glycidyl group and mercapto group are kneaded and formed in an extruder under following conditions. Namely, the ethylene-vinyl acetate copolymer is supplied to the raw material inlet of the extruder, the condensation reaction product and silane coupling agent are supplied to the raw material inlet or a raw material inlet separately provided after the inlet, and the specific power shown by E=(capacitance of driving motor) (load current value/rated current value) (revolving speed/maximum revolving speed/(actual extrusion output) is controlled to 0.2-0.35kw.h/kg.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、合わせガラス用中間膜
の製造方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing an interlayer film for laminated glass.

【0002】[0002]

【従来の技術】従来より、自動車、飛行機などに使用さ
れている風防用ガラスや、建築物の窓ガラスに使用され
ている積層ガラスは、2枚の相対するガラス板間にポリ
ビニルブチラール樹脂からなる中間膜を挟んだサンドイ
ッチ構造物が用いられている。しかしながら、ポリビニ
ルブチラール樹脂の中間膜は、保存時にブロッキングを
起こしたり、合わせ加工によりサンドイッチ構造物を製
造する作業が煩雑であるという問題点があった。
2. Description of the Related Art Conventionally, windshield glass used for automobiles and airplanes, and laminated glass used for window glass of buildings are made of polyvinyl butyral resin between two opposing glass plates. A sandwich structure sandwiching an intermediate film is used. However, the polyvinyl butyral resin interlayer film has a problem that blocking occurs during storage and the work of manufacturing a sandwich structure by a laminating process is complicated.

【0003】上記問題点を解決するために、エチレン−
酢酸ビニル共重合体を用いた中間膜が提案されている
(特公昭47−2103号公報)。しかしながら、中間
膜の透明性を確保し劣化を防止するために、ロールミル
等で低温において高混練した後、押出機でシート状に成
形するので、製造工程が2工程となって煩雑であり、生
産性が低下するという問題点があった。
In order to solve the above problems, ethylene-
An intermediate film using a vinyl acetate copolymer has been proposed (Japanese Patent Publication No. 47-2103). However, in order to secure the transparency of the interlayer film and prevent deterioration, it is complicatedly kneaded at a low temperature in a roll mill or the like and then formed into a sheet by an extruder, which makes the manufacturing process complicated in two steps. However, there is a problem in that

【0004】[0004]

【発明が解決しようとする課題】本発明は、上記問題点
に鑑みてなされたものであって、その目的は、混練と押
出成形とを同一工程で行うことができる合わせガラス用
中間膜の製造方法を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and an object of the present invention is to produce an interlayer film for laminated glass in which kneading and extrusion molding can be performed in the same step. To provide a method.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

【0006】第1発明の合わせガラス用中間膜の製造方
法は、エチレン−酢酸ビニル共重合体と、5価以上のア
ルコールとベンズアルデヒドの縮合反応生成物と、アミ
ノ基、グリシジル基及びメルカプト基からなる群より選
ばれる1種以上の基を有するシランカップリング剤とを
押出機に供給して混練成形する際に、前記エチレン−酢
酸ビニル共重合体を押出機の原料供給部から押出機に供
給すると共に、前記縮合反応生成物及びシランカップリ
ング剤を、該原料供給部(I)又は該原料供給部(I)
以降に別途設けられた原料供給部(II)から押出機に供給
し、下式で表される押出機の駆動モーターの比動力
(E)が0.2〜0.35〔kw・h/kg〕の範囲で
押出成形することを特徴とする。
The method for producing an interlayer film for laminated glass of the first invention comprises an ethylene-vinyl acetate copolymer, a condensation reaction product of an alcohol having a valence of 5 or more and benzaldehyde, an amino group, a glycidyl group and a mercapto group. When the silane coupling agent having at least one group selected from the group is supplied to the extruder for kneading and molding, the ethylene-vinyl acetate copolymer is supplied to the extruder from the raw material supply section of the extruder. Together with the condensation reaction product and the silane coupling agent, the raw material supply section (I) or the raw material supply section (I)
It is supplied to the extruder from a raw material supply section (II) separately provided thereafter, and the specific power (E) of the drive motor of the extruder represented by the following formula is 0.2 to 0.35 [kw · h / kg ] Extrusion molding is characterized by the range.

【0007】第2発明の合わせガラス用中間膜の製造方
法は、請求項1において、押出成形時に押出機に設けら
れたベント部より真空吸引することを特徴とする。
The method for producing an interlayer film for laminated glass according to the second aspect of the present invention is characterized in that, in claim 1, vacuum suction is performed from a vent portion provided in the extruder during extrusion molding.

【0008】以下、第1発明を詳細に説明する。The first invention will be described in detail below.

【0009】第1発明で使用されるエチレン−酢酸ビニ
ル共重合体(以下EVAという)としては、特に限定さ
れないが、酢酸ビニル含有量が少なくなると合わせガラ
スの透明性が低下し、多くなると合わせガラスの耐衝撃
性が低下するので、15〜45重量%が好ましい。
The ethylene-vinyl acetate copolymer (hereinafter referred to as EVA) used in the first invention is not particularly limited, but when the vinyl acetate content is low, the transparency of the laminated glass is low, and when it is high, the laminated glass is high. 15 to 45% by weight is preferable because the impact resistance of (1) decreases.

【0010】第1発明で使用される5価以上のアルコー
ルとベンズアルデヒドの縮合反応生成物としては、例え
ば、ジベンジリデンソルビトール、ジベンジリデンキシ
リトール、ジベンジリデンズルシトール、ジベンジリデ
ンマンニトール、ビス(パラメチルベンジリデン)ソル
ビトール等があげられる。
Examples of the condensation reaction product of a pentavalent or more alcohol and benzaldehyde used in the first invention include dibenzylidene sorbitol, dibenzylidene xylitol, dibenzylidene lucitol, dibenzylidene mannitol, bis (paramethylbenzylidene). ) Sorbitol and the like.

【0011】第1発明で使用されるシランカップリング
剤としては、アミノ基、グリシジル基及びメルカプト基
からなる群より選ばれる1種以上の基を有するものであ
って、例えば、N−(2−アミノエチル)−3−アミノ
プロピルメチルジメトキシシラン、3−アミノプロピル
トリメトキシシラン、3−アミノプロピルトリエトキシ
シラン、3−グリシドキシプロピルジメチルエトキシシ
ラン、(3−グリドキシプロピル)メチルジエトキシシ
ラン、3−グリドキシプロピルトリメトキシシラン、3
−メルカプトプロピルトリメトキシシラン、3−メルカ
プトプロピルメチルジメトキシシランなどが挙げられ
る。
The silane coupling agent used in the first invention has at least one group selected from the group consisting of an amino group, a glycidyl group and a mercapto group, and is, for example, N- (2- Aminoethyl) -3-aminopropylmethyldimethoxysilane, 3-aminopropyltrimethoxysilane, 3-aminopropyltriethoxysilane, 3-glycidoxypropyldimethylethoxysilane, (3-glydoxypropyl) methyldiethoxysilane, 3-glydoxypropyltrimethoxysilane, 3
-Mercaptopropyltrimethoxysilane, 3-mercaptopropylmethyldimethoxysilane and the like can be mentioned.

【0012】次に、上記エチレン−酢酸ビニル共重合体
と、5価以上のアルコールとベンズアルデヒドの縮合反
応生成物及びシランカップリング剤から、合わせガラス
用中間膜を押出成形により製造する方法について、図を
参照しながら説明する。図1は、本発明の製造方法に使
用される押出機を示す模式図である。
Next, a method for producing an interlayer film for laminated glass from the above ethylene-vinyl acetate copolymer, a condensation reaction product of a pentavalent or more alcohol and benzaldehyde, and a silane coupling agent by extrusion molding will be described. Will be described with reference to. FIG. 1 is a schematic diagram showing an extruder used in the manufacturing method of the present invention.

【0013】まず、EVA共重合体を、EVA共重合体
用フィーダー5から押出機1に設けられた原料供給部
(I)3から押出機1へ供給し、続いて、5価以上のア
ルコールとベンズアルデヒドとの縮合反応生成物を、該
縮合反応生成物フィーダー6より原料供給部(I)3又
は該原料供給部(I)3以降に別途設けられた原料供給
部(II) 4から押出機1へ供給し、さらに、シランカッ
プリング剤を原料供給部(I)3又は原料供給部(II)
4から押出機1へ供給して押出成形する。
First, the EVA copolymer is supplied from the EVA copolymer feeder 5 to the extruder 1 from the raw material supply section (I) 3 provided in the extruder 1, and subsequently, with an alcohol having a valence of 5 or more. The condensation reaction product with benzaldehyde is fed from the condensation reaction product feeder 6 to the raw material supply section (I) 3 or a raw material supply section (II) 4 separately provided after the raw material supply section (I) 3 to the extruder 1 To the raw material supply part (I) 3 or the raw material supply part (II).
4 to the extruder 1, and extrusion molding is performed.

【0014】上記押出成形において、押出機の駆動モー
ターの比動力(E)が、小さくなると所定の透明性(ヘ
イズ値1.1未満)が得られず、得られた合わせガラス
が曇りを生じ、大きくなるとシランカップリング剤の混
練過多による熱分解で黄変するため、比動力(E)0.
2〜0.35〔kw・h/kg〕の範囲で押出成形す
る。
In the above extrusion molding, when the specific power (E) of the driving motor of the extruder becomes small, the predetermined transparency (haze value less than 1.1) cannot be obtained, and the obtained laminated glass becomes cloudy, When it becomes larger, the specific power (E) becomes less than 0.8 because the silane coupling agent becomes yellow due to thermal decomposition due to excessive kneading.
Extrusion is performed in the range of 2 to 0.35 [kW · h / kg].

【0015】上記の条件で、押出機内で混練成形された
組成物を、ベント部7で脱気し金型8にてシート状に賦
形した後、引き取りロール9で冷却することにより、合
わせガラス用中間膜10が得られる。
The composition kneaded and molded in the extruder under the above-described conditions is degassed at the vent portion 7, shaped into a sheet by the die 8, and then cooled by the take-up roll 9 to obtain a laminated glass. The intermediate film 10 for use is obtained.

【0016】尚、上記押出機の駆動モーターの比動力
(E)は、混練量を示す指標であって、次式で表される
値である。 E〔kw・h/kg〕=(駆動モーターの電気容量)×
(負荷電流値/定格電流値)×(回転数/最大回転数)
/(実押出量)
The specific power (E) of the driving motor of the extruder is an index showing the kneading amount, and is a value represented by the following equation. E [kW / h / kg] = (electric capacity of drive motor) ×
(Load current value / Rated current value) x (Rotation speed / Maximum rotation speed)
/ (Actual extrusion amount)

【0017】実際の製造工程では、押出機の駆動モータ
ーの比動力(E)が上記数値範囲となるように、押出機
の供給量、シリンダー温度、スクリュー回転数等を調整
して押出成形を行う。上記押出機としては、単軸あるい
は二軸以上の多軸押出機のいずれのタイプも使用可能で
あり、スクリューの形状についても特に制限されない。
In the actual manufacturing process, extrusion molding is carried out by adjusting the supply amount of the extruder, the cylinder temperature, the screw rotation speed, etc. so that the specific power (E) of the drive motor of the extruder falls within the above numerical range. . As the extruder, any type of a single-screw or a multi-screw extruder having two or more screws can be used, and the shape of the screw is not particularly limited.

【0018】以下、第2発明について説明する。第2発
明の合わせガラス用中間膜の製造方法は、EVA共重合
体の押出成形において、図1に示された押出機1のベン
ト部7から真空吸引を行う点が第1発明と異なる。真空
吸引における真空度は、600mmHg以上が好まし
く、より好ましくは700mmHg以上である。
The second invention will be described below. The method for producing an interlayer film for laminated glass of the second invention is different from the first invention in that, in extrusion molding of EVA copolymer, vacuum suction is performed from the vent portion 7 of the extruder 1 shown in FIG. The degree of vacuum in vacuum suction is preferably 600 mmHg or more, more preferably 700 mmHg or more.

【0019】[0019]

【作用】第1発明の合わせガラス用中間膜の製造方法に
おいて、駆動モーターの比動力(E)を0.2〜0.3
5〔kw・h/kg〕の範囲で混練することにより、5
価以上のアルコールとベンズアルデヒドとの縮合反応生
成物は、微小、均質に分散されてEVA共重合体の結晶
単位を透過光線の波長以下とするための核剤となり、合
わせガラス用中間膜に優れた透明性を付与する。また、
第1発明の合わせガラス用中間膜の製造方法では、組成
物中にシランカップリング剤を添加することにより、ガ
ラス板に対する接着性の優れた中間膜を提供する。
In the method for producing an interlayer film for laminated glass according to the first aspect of the present invention, the specific power (E) of the drive motor is 0.2 to 0.3.
By kneading in the range of 5 [kW · h / kg], 5
The condensation reaction product of an alcohol having a valence higher than or equal to benzaldehyde is finely and homogeneously dispersed to serve as a nucleating agent for keeping the crystal units of the EVA copolymer at the wavelength of the transmitted light or less, and is excellent as an interlayer film for laminated glass. Adds transparency. Also,
In the method for producing an interlayer film for laminated glass according to the first aspect of the present invention, by adding a silane coupling agent to the composition, an interlayer film having excellent adhesiveness to a glass plate is provided.

【0020】第2発明の合わせガラス用中間膜の製造方
法では、シランカップリング剤が酸素存在下で熱安定性
が悪く樹脂温度に敏感に反応するため、駆動モーターの
比動力(E)を0.2〜0.35〔kw・h/kg〕の
範囲で混練することにより混練過多による発熱が抑制さ
れ、さらにベント部からの真空吸引により、中間膜の黄
変を防止しうる。
In the method for producing an interlayer film for laminated glass according to the second aspect of the invention, the silane coupling agent has poor thermal stability in the presence of oxygen and is sensitive to the resin temperature, so that the specific power (E) of the drive motor is 0. By kneading in the range of 0.2 to 0.35 [kW / h / kg], heat generation due to excessive kneading can be suppressed, and further vacuum suction from the vent portion can prevent yellowing of the interlayer film.

【0021】[0021]

【実施例】【Example】

(実施例1、2及び比較例1〜3)EVA共重合体(住
友化学社製「エバテート5011」)100重量部を、
図1に示したフィーダー5から原料供給部(I)3へ供
給し、ジベンジリデンソルビトール(新日本理化学社製
「ゲルオールD」)0.3重量部をフィーダー6から原
料供給部(I)3へ供給し、さらにシランカップリング
剤0.05重量部を原料供給部(II)4へ供給して、表
1に示した所定の押出条件で合わせガラス用中間膜を押
出成形した。 ・押出機の仕様 東芝機械社製二軸同方向回転押出機、スクリュー:13
0mmφ、L=1800mm 駆動モーターの電気容量:37kw、最大回転数:15
00rpm
(Examples 1 and 2 and Comparative Examples 1 to 3) 100 parts by weight of EVA copolymer (“Evatate 5011” manufactured by Sumitomo Chemical Co., Ltd.)
The raw material is supplied from the feeder 5 shown in FIG. 1 to the raw material supply section (I) 3, and 0.3 parts by weight of dibenzylidene sorbitol (“Gel All D” manufactured by Shin Nihon Riken Co., Ltd.) is fed from the feeder 6 to the raw material supply section (I) 3. Then, 0.05 part by weight of the silane coupling agent was supplied to the raw material supply section (II) 4, and the interlayer film for laminated glass was extrusion-molded under the predetermined extrusion conditions shown in Table 1.・ Extruder specifications Toshiba Machinery twin-screw co-rotating extruder, screw: 13
0mmφ, L = 1800mm Electric capacity of drive motor: 37kw, maximum rotation speed: 15
00 rpm

【0022】(実施例3、4及び比較例4、5)押出機
のベント部から真空吸引しながら表2に示した所定の押
出条件で押出成形したこと以外は、実施例1と同様にし
て、合わせガラス用中間膜を得た。
(Examples 3 and 4 and Comparative Examples 4 and 5) The same procedure as in Example 1 was carried out except that extrusion molding was performed under the predetermined extrusion conditions shown in Table 2 while vacuum sucking from the vent portion of the extruder. An intermediate film for laminated glass was obtained.

【0023】合わせガラス用中間膜の性能評価 上記実施例及び比較例で得られた合わせガラス用中間膜
につき、下記の性能評価を行いその結果を表1及び2に
示した。 (1)透明性 上記合わせガラス用中間膜(0.8mm厚)を二枚のガ
ラス板(2.5mm厚)に挟み込んで合わせガラスを作
製した後、この合わせガラスにつき、東京電色社製「積
分式濁度計」を用いてヘイズ値を測定し、ヘイズ値1.
0以下を透明性良好と判定した。 (2)着色性 (1)と同様にして作製した合わせガラスにつき、東京
電色社製「色差計」を用いてJIS K7103に準拠
して黄色度(YI)を測定し、黄色度3.0以下を着色
なしと判定した。
Performance Evaluation of Interlayer Film for Laminated Glass The interlayer film for laminated glass obtained in the above Examples and Comparative Examples was subjected to the following performance evaluation and the results are shown in Tables 1 and 2. (1) Transparency After sandwiching the interlayer film for laminated glass (0.8 mm thickness) between two glass plates (2.5 mm thickness) to prepare laminated glass, the laminated glass is manufactured by Tokyo Denshoku Co., Ltd. The haze value was measured using an "integration type turbidimeter".
A transparency of 0 or less was determined to be good. (2) Colorability The yellowness (YI) of the laminated glass produced in the same manner as in (1) was measured using a "color difference meter" manufactured by Tokyo Denshoku Co., Ltd. according to JIS K7103, and the yellowness was 3.0. The following was judged to have no color.

【0024】[0024]

【表1】 [Table 1]

【0025】[0025]

【表2】 [Table 2]

【0026】[0026]

【発明の効果】第1発明の合わせガラス用中間膜の製造
方法は、上述の通りであり、エチレン−酢酸ビニル共重
合体に、5価以上のアルコールとベンズアルデヒドの縮
合反応生成物及びシランカップリング剤を添加し、押出
機の駆動モーターの比動力(E)が0.20〜0.35
〔kw・h/kg〕となるような成形条件で押出成形す
ることにより、混練と押出成形を同一工程で行うことが
でき、シランカップリング剤の熱分解による着色がな
く、透明性に優れた合わせガラス用中間膜を直接押出成
形することができる。
The method for producing an interlayer film for laminated glass according to the first aspect of the present invention is as described above, in which an ethylene-vinyl acetate copolymer is added to a condensation reaction product of a pentavalent or higher alcohol and benzaldehyde and silane coupling. The specific power (E) of the driving motor of the extruder is 0.20 to 0.35 by adding the agent.
By extrusion molding under the molding conditions such that [kw · h / kg], kneading and extrusion molding can be performed in the same step, and there is no coloring due to thermal decomposition of the silane coupling agent, resulting in excellent transparency. The interlayer film for laminated glass can be directly extruded.

【0027】第2発明の合わせガラス用中間膜の製造方
法は、上述の通りであり、エチレン−酢酸ビニル共重合
体に、5価以上のアルコールとベンズアルデヒドの縮合
反応生成物及びシランカップリング剤を添加し、ベント
部から真空吸引しながら押出機の駆動モーターの比動力
(E)が0.20〜0.35〔kw・h/kg〕となる
ような成形条件で押出成形することにより、混練と押出
成形を同一工程で行うことができ、シランカップリング
剤の熱分解による着色が改善され、透明性に優れた合わ
せガラス用中間膜を直接押出成形することができる。
The method for producing an interlayer film for laminated glass of the second invention is as described above, and the ethylene-vinyl acetate copolymer is provided with a condensation reaction product of a pentavalent or higher alcohol and benzaldehyde and a silane coupling agent. Kneading by adding and extruding under a molding condition such that the specific power (E) of the drive motor of the extruder is 0.20 to 0.35 [kw · h / kg] while vacuum suction from the vent part. And extrusion molding can be carried out in the same step, the coloring due to thermal decomposition of the silane coupling agent is improved, and the interlayer film for laminated glass having excellent transparency can be directly extrusion molded.

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

【図1】第1及び第2発明の製造方法で使用される押出
機を示す模式図である。
FIG. 1 is a schematic view showing an extruder used in the manufacturing methods of the first and second inventions.

【符号の説明】[Explanation of symbols]

1 押出機 2 駆動モーター 3 原料供給部(I) 4 原料供給部(II) 5,6 フィーダー 7 ベント部 8 金型 9 引き取りロール 10 中間膜 DESCRIPTION OF SYMBOLS 1 Extruder 2 Drive motor 3 Raw material supply part (I) 4 Raw material supply part (II) 5,6 Feeder 7 Vent part 8 Mold 9 Take-off roll 10 Intermediate film

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】エチレン−酢酸ビニル共重合体と、5価以
上のアルコールとベンズアルデヒドの縮合反応生成物
と、アミノ基、グリシジル基及びメルカプト基からなる
群より選ばれる1種以上の基を有するシランカップリン
グ剤とを押出機に供給して混練成形する際に、前記エチ
レン−酢酸ビニル共重合体を押出機の原料供給部から押
出機に供給すると共に、前記縮合反応生成物及びシラン
カップリング剤を、該原料供給部(I)又は該原料供給
部(I)以降に別途設けられた原料供給部(II)から押出
機に供給し、下式で表される押出機の駆動モーターの比
動力(E)が0.2〜0.35〔kw・h/kg〕の範
囲で押出成形することを特徴とする合わせガラス用中間
膜の製造方法。 E=(駆動モーターの電気容量)×(負荷電流値/定格
電流値)×(回転数/最大回転数)/(実押出量)
1. A silane having an ethylene-vinyl acetate copolymer, a condensation reaction product of a pentavalent or more alcohol and benzaldehyde, and at least one group selected from the group consisting of an amino group, a glycidyl group and a mercapto group. When supplying a coupling agent and kneading and molding to an extruder, the ethylene-vinyl acetate copolymer is supplied to the extruder from a raw material supply unit of the extruder, and the condensation reaction product and the silane coupling agent are also supplied. Is supplied to the extruder from the raw material supply unit (I) or a raw material supply unit (II) separately provided after the raw material supply unit (I), and the specific power of the drive motor of the extruder represented by the following formula A method for producing an interlayer film for laminated glass, which comprises subjecting (E) to extrusion molding in a range of 0.2 to 0.35 [kW · h / kg]. E = (electric capacity of drive motor) × (load current value / rated current value) × (rotation speed / maximum rotation speed) / (actual extrusion amount)
【請求項2】押出成形時に押出機に設けられたベント部
より真空吸引することを特徴とする請求項1記載の合わ
せガラス用中間膜の製造方法。
2. The method for producing an interlayer film for laminated glass according to claim 1, wherein vacuum suction is performed from a vent portion provided in the extruder during extrusion molding.
JP6152030A 1993-12-03 1994-07-04 Production of intermediate film for laminated glass Pending JPH07206484A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6152030A JPH07206484A (en) 1993-12-03 1994-07-04 Production of intermediate film for laminated glass

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP30389693 1993-12-03
JP5-303896 1993-12-03
JP6152030A JPH07206484A (en) 1993-12-03 1994-07-04 Production of intermediate film for laminated glass

Publications (1)

Publication Number Publication Date
JPH07206484A true JPH07206484A (en) 1995-08-08

Family

ID=26481073

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6152030A Pending JPH07206484A (en) 1993-12-03 1994-07-04 Production of intermediate film for laminated glass

Country Status (1)

Country Link
JP (1) JPH07206484A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015152275A1 (en) * 2014-03-31 2015-10-08 積水化学工業株式会社 Intermediate film for laminated glass, method for manufacturing intermediate film for laminated glass, and laminated glass

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015152275A1 (en) * 2014-03-31 2015-10-08 積水化学工業株式会社 Intermediate film for laminated glass, method for manufacturing intermediate film for laminated glass, and laminated glass
JP5855796B1 (en) * 2014-03-31 2016-02-09 積水化学工業株式会社 Intermediate film for laminated glass, method for producing interlayer film for laminated glass, and laminated glass
JP2016108239A (en) * 2014-03-31 2016-06-20 積水化学工業株式会社 Interlayer for laminated glass, method for producing interlayer for laminated glass and laminated glass
RU2666434C2 (en) * 2014-03-31 2018-09-07 Секисуй Кемикал Ко., Лтд. Intermediate film for laminated glass, method for manufacturing intermediate film for laminated glass, and laminated glass
US11014339B2 (en) 2014-03-31 2021-05-25 Sekisui Chemical Co., Ltd. Intermediate film for laminated glass, method for manufacturing intermediate film for laminated glass, and laminated glass

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