JPS6234624B2 - - Google Patents
Info
- Publication number
- JPS6234624B2 JPS6234624B2 JP55143213A JP14321380A JPS6234624B2 JP S6234624 B2 JPS6234624 B2 JP S6234624B2 JP 55143213 A JP55143213 A JP 55143213A JP 14321380 A JP14321380 A JP 14321380A JP S6234624 B2 JPS6234624 B2 JP S6234624B2
- Authority
- JP
- Japan
- Prior art keywords
- polyethylene terephthalate
- terephthalate resin
- stretched
- intrinsic viscosity
- value
- 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
Links
Landscapes
- Package Frames And Binding Bands (AREA)
- Shaping Of Tube Ends By Bending Or Straightening (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Description
(産業上の利用分野)
本発明はポリエチレンテレフタレート樹脂製荷
造りバンド及びその製造方法に関する。
(従来の技術)
重量の大きい重梱包品の結束帯として天然繊維
や合成繊維を加工した結束帯、あるいは鋼鉄製の
結束帯がある。前者は結束後の応力緩和による荷
くずれ、張力や結節強力不足による切断等の欠点
があり、後者は腐蝕の問題や解梱包の際等の危険
性の問題があつた。
そこで、これらに代わる結束帯として、ポリエ
チレンテレフタレート樹脂製の荷造りバンドが考
えられた。従来のポリエチレンテレフタレート樹
脂製のバンドは、主に一段延伸成形されており、
又原材料として固有粘度(IV値)0.90以下のポリ
エチレンテレフタレート樹脂が用いられている。
(発明が解決しようとする問題点)
しかしながら、次の各欠点を有する。(a)強度が
不足する。(b)ヒートシール強度が小さくヒートシ
ールにばらつきが多い。(c)高温における収縮率が
大きく高温な場所での使用ができない。(d)耐候性
が劣る。
等の欠点がある。
ポリエチレンテレフタレート樹脂の二段延伸成
形は過去に何件か提案されているが、フイルムの
透明度を出すことをねらいとしたものが多く、前
記と同様な欠点の他にたて割れする等の欠点があ
る。
(問題点を解決するための手段)
発明者は、従来のポリエチレンテレフタレート
成形物が上記のような多くの欠点を有するのは、
樹脂粘度の問題と二段延伸条件であることに着目
し本発明の創作に至つた。本発明は原料の固有粘
度(IV値)が0.90〜1.20のポリエチレンテレフタ
レート樹脂製帯状体であつて、長さ方向に延伸さ
れた全延伸倍率が3〜6倍とされたポリエチレン
テレフタレート樹脂製荷造りバンド、及び押出機
の除湿機付乾燥ホツパーにて乾燥した固有粘度
(IV値)が0.90〜1.20のポリエチレンテレフタレ
ートを金型より熔融押出し、この押出した熔融樹
脂を第一水槽内で冷却して帯状体とし、この帯状
体を第一段延伸として85〜100℃の温度で延伸倍
率3〜4.5倍に延伸し、続いて第二段延伸として
250〜350℃の高温度で延伸して長さ方向の全延伸
倍率を4.6〜6倍とし、更に温度180〜280℃の熱
処理槽内をダウン率0〜5%の引取速度で通過さ
せて熱処理するポリエチレンテレフタレート樹脂
製荷造りバンドの製造方法よりなるものである。
(作用)
固有粘度(IV値)が0.90〜1.20のポリエチレン
テレフタレート樹脂を用いることにより、ヒート
シール性がよく、また、全延伸倍率が3〜6倍と
されてたて割れ、延伸切断が生じることなく強度
が向上される。二段延伸成形は繊維軸と直角方向
及び軸方向の結晶化を進め、二段延伸された後の
熱処理により波打つている歪がとられ、結晶化が
促進される。
(実施例)
以下本発明ポリエチレンテレフタレート樹脂製
荷造りバンド及びその製造方法につき詳細に説明
する。
原材料として固有粘度(IV値)0.90〜1.20のポ
リエチレンテレフタレート樹脂を用いる。押出機
2の除湿機付乾燥ホツパー1にて150℃の温度で
約4時間乾燥して水分を0.02%以下とした固有粘
度0.90〜1.20のポリエチレンテレフタレートを
240〜285℃に設定したシリンダーを経て金型3よ
り熔融押出す。この押出した溶融樹脂を水温50℃
に設定した第一水槽4で冷却した後第一引取機5
に引取り帯状体6となす。この帯状体6は第一延
伸槽7内を通過して第二引取機8に引取る。第一
延伸槽7内では帯状体6を熱水または蒸気で85〜
100℃に加熱し、延伸倍率3〜4.5とする。延伸は
第一引取機5と第二引取機8との回転速度を調整
することにより行なう。このように延伸した帯状
体6は更に第二延伸槽9を通過して第三引取機1
0に送る。この第二延伸槽9内では電気ヒーター
または熱風等による乾式加熱で帯状体6を250〜
350℃の高温雰囲気で加熱し、延伸倍率を1.2〜
1.5とする。尚、第一段延伸とのトータルの長さ
方向への延伸倍率は4.6〜6である。延伸倍率4.6
以下のとき充分な強度がえられず、とくに3以下
のときは所期の強度えられない。また延伸倍率6
以上の場合たて割れ、延伸切断が生じる。
このように二段延伸した帯状体はバンド15と
なり、このバンドはエンボスロール11にてエン
ボス加工をして帯状体の長さ方向に整つた分子配
向を乱し、熱処理槽12内を通過させて乾式ヒー
ター180〜280℃にて熱処理し、第二冷却槽13に
て冷却の後、第四引取機14を経て巻取装置16
にて巻取る。尚、第三引取機10と第四引取機1
4との引取スピード比は同速もしくは第四引取機
14の引取スピードを約5%ダウンさせる。
二段延伸した後、熱処理を行つている。これは
配向によつて波打つている歪をとると共に、結晶
化を促進させる効果がある。ダウン率は通常0〜
5%で、熱処理槽通過の際バンドに余り張力がか
からないように設定する。ダウンさせずに熱処理
したバンドを巻取ドラムに巻取ると、巻取つた後
にバンドが収縮してバンドを支える紙管が破壊さ
れる等の問題を生じる。
次に上記の方法で製造したポリエチレンテレフ
タレート製バンドと、樹脂の固有粘度を本発明
と同じくし一段延伸したポリエチレンテレフタレ
ート製バンドと、固有粘度0.90以下で二段延伸
したポリエチレンテレフタレート製バンドと、
固有粘度0.90以下で一段延伸したポリエチレンテ
レフタレート製バンドとを物性比較した表1に
示す。尚、いずれも巾が16mm、厚みが0.6mmのバ
ンドである。
(Industrial Application Field) The present invention relates to a packing band made of polyethylene terephthalate resin and a method for manufacturing the same. (Prior Art) Binding bands for heavy packaged items include binding bands made of processed natural fibers or synthetic fibers, and binding bands made of steel. The former has disadvantages such as load collapse due to stress relaxation after bundling and breakage due to insufficient tension and knot strength, while the latter has problems of corrosion and danger when unpacking. Therefore, packing bands made of polyethylene terephthalate resin were considered as an alternative binding band. Conventional bands made of polyethylene terephthalate resin are mainly one-step stretch molded.
In addition, polyethylene terephthalate resin with an intrinsic viscosity (IV value) of 0.90 or less is used as a raw material. (Problems to be Solved by the Invention) However, it has the following drawbacks. (a) Insufficient strength. (b) Heat sealing strength is low and there are many variations in heat sealing. (c) The shrinkage rate at high temperatures is large and it cannot be used in high temperature locations. (d) Poor weather resistance. There are drawbacks such as. Several proposals have been made for two-stage stretch molding of polyethylene terephthalate resin in the past, but most of them were aimed at increasing the transparency of the film, and in addition to the same drawbacks as mentioned above, they also have drawbacks such as vertical cracking. be. (Means for Solving the Problems) The inventor believes that the reason why conventional polyethylene terephthalate molded products have many drawbacks as described above is that
The present invention was created by focusing on the problem of resin viscosity and the two-stage stretching conditions. The present invention is a polyethylene terephthalate resin band whose raw material has an inherent viscosity (IV value) of 0.90 to 1.20, and the polyethylene terephthalate resin packing band is stretched in the length direction at a total stretching ratio of 3 to 6 times. , and polyethylene terephthalate with an intrinsic viscosity (IV value) of 0.90 to 1.20, dried in a drying hopper with a dehumidifier of an extruder, is melt-extruded from a mold, and the extruded molten resin is cooled in a first water tank to form a strip. This strip-shaped body is stretched at a temperature of 85 to 100°C to a stretching ratio of 3 to 4.5 times as the first stage of stretching, and then as the second stage of stretching.
Stretched at a high temperature of 250 to 350°C to give a total stretching ratio of 4.6 to 6 times in the length direction, and then heat treated by passing through a heat treatment tank at a temperature of 180 to 280°C at a take-up speed with a down rate of 0 to 5%. A method for manufacturing a packing band made of polyethylene terephthalate resin. (Function) By using polyethylene terephthalate resin with an intrinsic viscosity (IV value) of 0.90 to 1.20, it has good heat sealing properties, and the total stretching ratio is 3 to 6 times, which prevents vertical cracking and stretch breakage. strength is improved. The two-stage stretching process promotes crystallization in the direction perpendicular to the fiber axis and in the axial direction, and the heat treatment after the two-stage stretching removes the undulating distortion and promotes crystallization. (Example) The packing band made of polyethylene terephthalate resin of the present invention and the manufacturing method thereof will be described in detail below. Polyethylene terephthalate resin with an intrinsic viscosity (IV value) of 0.90 to 1.20 is used as a raw material. Polyethylene terephthalate with an intrinsic viscosity of 0.90 to 1.20 is dried at a temperature of 150°C for about 4 hours in the drying hopper 1 with a dehumidifier of the extruder 2 to reduce the moisture content to 0.02% or less.
The melt is extruded from mold 3 through a cylinder set at 240-285°C. This extruded molten resin is heated to a water temperature of 50℃.
After cooling in the first water tank 4 set to
Then, it is taken up and made into a strip 6. This strip-shaped body 6 passes through a first drawing tank 7 and is taken up by a second taking-off machine 8 . In the first drawing tank 7, the strip 6 is heated to 85°C or more with hot water or steam.
It is heated to 100°C and the stretching ratio is 3 to 4.5. Stretching is performed by adjusting the rotational speeds of the first drawing machine 5 and the second drawing machine 8. The thus stretched strip 6 further passes through a second stretching tank 9 and is transferred to a third drawing machine 1.
Send to 0. In this second drawing tank 9, the strip 6 is heated to a temperature of 250 to
Heating in a high temperature atmosphere of 350℃, stretching ratio is 1.2 ~
Set it to 1.5. Incidentally, the total stretching ratio in the length direction including the first stage stretching is 4.6 to 6. Stretching ratio 4.6
In the following cases, sufficient strength cannot be obtained, and in particular, in the case of 3 or less, the desired strength cannot be obtained. Also, the stretching ratio is 6
In the above cases, vertical cracks and stretch cuts occur. The belt-shaped body stretched in two stages in this way becomes a band 15, which is embossed with an embossing roll 11 to disturb the molecular orientation arranged in the length direction of the belt-shaped body, and then passed through a heat treatment tank 12. After being heat treated with a dry heater at 180 to 280°C and cooled in a second cooling tank 13, it is passed through a fourth take-up machine 14 to a take-up device 16.
Wind it up. In addition, the third collection machine 10 and the fourth collection machine 1
The take-up speed ratio with No. 4 is the same or the take-up speed of the fourth take-up machine 14 is reduced by about 5%. After two-stage stretching, heat treatment is performed. This has the effect of removing undulating distortion due to orientation and promoting crystallization. Down rate is usually 0~
5% so that the band does not have too much tension when passing through the heat treatment tank. If a heat-treated band is wound onto a winding drum without being rolled down, problems such as shrinkage of the band after winding and destruction of the paper tube supporting the band will occur. Next, a band made of polyethylene terephthalate produced by the above method, a band made of polyethylene terephthalate that was stretched in one step with the same intrinsic viscosity as the present invention, and a band made of polyethylene terephthalate that was stretched in two steps with an intrinsic viscosity of 0.90 or less,
Table 1 shows a comparison of physical properties with a polyethylene terephthalate band that has been stretched in one step with an intrinsic viscosity of 0.90 or less. Both bands are 16mm wide and 0.6mm thick.
【表】
この表1で示したように、本発明方法で製造し
たポリエチレンテレフタレート樹脂製バンドは引
張強度、融着強度がよく、収縮率が低く、耐候性
がよく、たて割れしない。
固有粘度(IV値)の高いポリエチレンテレフ
タレート樹脂を用いているため、ヒートシール性
がよく、また、高倍率延伸であるがたて割れせず
強度が向上できる。一方、ポリエチレンテレフタ
レート樹脂は、150℃以上の温度で延伸すること
により繊維軸方向の配向結晶化が進み強度アツプ
する。本発明の第二延伸成形では、繊維軸と直角
方向の結晶化(一段目)、繊維軸方向の結晶化
(二段目)を各行程で進め、また、延伸歪を除去
する行程(熱処理)を別に設けることにより、た
て割れがなく、強度が大きく、高温における収縮
率の少ないバンドとなる。ポリエチレンテレフタ
レート樹脂製バンドの耐候性は、2年の屋外暴露
でも強度の低下は余りなく、他のプラスチツク製
バンドよりはるかに優れている。
尚、本発明に於いてとくに留意しなければなら
ないことは、ポリエチレンテレフタレート樹脂
が、テレフタル酸とエチレングリコールの重縮合
により製造されたもので加熱熔融下、水分が含ま
れると加水分解し粘度低下を招き品質上著るしく
低下をきたすことである。よつて通常の成形では
原料を除湿機付乾燥ホツパーにて150℃4時間以
上乾燥し原料の水分を0.02%以下としている。
次に示す(表2)は原料の乾燥状態を変え本発
明の製造条件(表3)に従い成形した時の物性を
あらわしている。は本発明の実施例に従い除湿
機付乾燥ホツパーにて150℃4時間乾燥したもの
である。は同じく除湿機付乾燥ホツパーにて
150℃30分間乾燥したもので原料水分が0.05%以
上となつている。は150℃6時間真空乾燥行な
い真空押出成形したもので、原料水分が0.005%
以下となつている。
以上の原料乾燥状態により成形した成形品(バ
ンド)の固有粘度には大きな差が見られる。固有
粘度0.9以下の原料を用いても原料乾燥状態を良
くすれば固有粘度低下を押さえることができ、物
性的にも固有粘度0.95以上の原料を用い通常の乾
燥を行なつた場合と同等のものが得られる。よ
つて成形品の品質は原料の固有粘度だけではなく
成形品の固有粘度によつても影響される。
通常の原料乾燥では押出成形で8〜10%の粘度
ダウンは避けられない。しかし、先の例のごと
く、技術的に原料の真空乾燥と真空押出成形とを
行い、乾燥時間を長くする。押出機のシリンダ
ー、金型の樹脂滞溜分を極力無くする。等により
粘度ダウンを5%以下におさえることができる。
本発明に於いて、原料の固有粘度(IV値)が
0.90〜1.20のポリエチレンテレフタレート樹脂を
使用し、又その成形品の固有粘度(IV値)がと
くに0.80以上が要請される理由も上記の点からで
ある。[Table] As shown in Table 1, the polyethylene terephthalate resin band produced by the method of the present invention has good tensile strength and fusion strength, low shrinkage rate, good weather resistance, and does not crack vertically. Because it uses polyethylene terephthalate resin with a high intrinsic viscosity (IV value), it has good heat-sealing properties, and even though it is stretched at a high magnification, there is no vertical cracking and the strength can be improved. On the other hand, when polyethylene terephthalate resin is stretched at a temperature of 150° C. or higher, oriented crystallization in the fiber axis direction progresses and the strength increases. In the second stretch forming of the present invention, crystallization in the direction perpendicular to the fiber axis (first stage) and crystallization in the direction of the fiber axis (second stage) are advanced in each step, and a step (heat treatment) to remove stretching strain. By separately providing a band, the band is free from vertical cracks, has high strength, and has a low shrinkage rate at high temperatures. The weather resistance of the polyethylene terephthalate resin band is far superior to other plastic bands, with no significant decrease in strength even after two years of outdoor exposure. It should be noted that in the present invention, the polyethylene terephthalate resin is produced by polycondensation of terephthalic acid and ethylene glycol, and when it is heated and melted, it will hydrolyze and cause a decrease in viscosity if it contains moisture. This results in a significant deterioration in quality. Therefore, in normal molding, the raw material is dried in a drying hopper equipped with a dehumidifier at 150°C for 4 hours or more to reduce the moisture content of the raw material to 0.02% or less. The following (Table 2) shows the physical properties when molded according to the manufacturing conditions of the present invention (Table 3) while changing the drying state of the raw materials. was dried at 150° C. for 4 hours in a drying hopper equipped with a dehumidifier according to an example of the present invention. is also used in a drying hopper with a dehumidifier.
The raw material moisture content is 0.05% or more when dried at 150℃ for 30 minutes. is vacuum extruded after vacuum drying at 150°C for 6 hours, and the raw material moisture content is 0.005%.
It is as below. There is a large difference in the intrinsic viscosity of the molded products (bands) formed depending on the raw material drying conditions described above. Even if raw materials with an intrinsic viscosity of 0.9 or less are used, the decrease in intrinsic viscosity can be suppressed by improving the drying conditions of the raw materials, and the physical properties are equivalent to those obtained by normal drying using raw materials with an intrinsic viscosity of 0.95 or higher. is obtained. Therefore, the quality of a molded article is affected not only by the intrinsic viscosity of the raw material but also by the intrinsic viscosity of the molded article. With normal raw material drying, it is unavoidable that the viscosity decreases by 8 to 10% during extrusion molding. However, as in the previous example, the raw materials are technically vacuum dried and vacuum extruded, which increases the drying time. Eliminate resin stagnation in the extruder cylinder and mold as much as possible. etc., it is possible to suppress the viscosity reduction to 5% or less. In the present invention, the intrinsic viscosity (IV value) of the raw material is
This is also the reason why polyethylene terephthalate resin with a molecular weight of 0.90 to 1.20 is used and the molded product is required to have an intrinsic viscosity (IV value) of 0.80 or more.
【表】【table】
【表】
(発明の効果)
以上のごとく本発明は、高粘度のポリエチレン
テレフタレート樹脂を用いることにより特徴ある
荷造りバンドとするものである。本発明バンドは
重梱包用として最適である。特に重量梱包物を自
動梱包機にて梱包する場合には、その良好なヒー
トシール性が作業能率を向上させており、又屋外
や高温な場所への長期間放置が可能である。
このようになる本発明バンドは引張強度、ヒー
トシール強度共に高く、たて割れせず、高温にお
ける経日変化(収縮)が小さく、耐候性の良好な
荷造りバンド及び製造方法で産業上利用価値の高
いものである。[Table] (Effects of the Invention) As described above, the present invention provides a distinctive packing band by using a high viscosity polyethylene terephthalate resin. The band of the present invention is most suitable for heavy-duty packaging. In particular, when packing heavy items using an automatic packing machine, its good heat-sealability improves work efficiency, and it can be left outdoors or in high-temperature locations for long periods of time. The band of the present invention has high tensile strength and heat sealing strength, does not crack vertically, has little aging (shrinkage) at high temperatures, has good weather resistance, and has industrial value due to its manufacturing method. It's expensive.
図面は本発明方法の製造工程を示す概略図であ
る。
1…ホツパー、2…押出機、3…金型、4…第
一水槽、5…第一引取機、6…帯状体、7…第一
延伸槽、8…第二引取機、9…第二延伸槽、10
…第三引取機、11…エンボスロール、12…熱
処理槽、13…第二冷却槽、14…第四引取機、
15…バンド、16…巻取装置。
The drawings are schematic diagrams showing the manufacturing process of the method of the present invention. DESCRIPTION OF SYMBOLS 1...Hopper, 2...Extruder, 3...Mold, 4...First water tank, 5...First take-off machine, 6...Strip body, 7...First drawing tank, 8...Second take-off machine, 9...Second Stretching tank, 10
...Third take-up machine, 11... Emboss roll, 12... Heat treatment tank, 13... Second cooling tank, 14... Fourth take-up machine,
15... Band, 16... Winding device.
Claims (1)
エチレンテレフタレート樹脂製帯状体であつて、
長さ方向に延伸されて全延伸倍率が3〜6倍とな
されたポリエチレンテレフタレート樹脂製荷造り
バンド。 2 原料の固有粘度(IV値)が0.90〜1.20のポリ
エチレンテレフタレート樹脂製帯状体であつて、
長さ方向に延伸されてその全延伸倍率が3〜6倍
となされ、更に該帯状体の全範囲にわたつて長さ
方向に整つた分子配向がエンボス加工により乱さ
れてなるポリエチレンテレフタレート樹脂製荷造
りバンド。 3 原料の固有粘度(IV値)が0.90〜1.20で、最
終成形品の固有粘度(IV値)が0.80以上のポリエ
チレンテレフタレート樹脂製帯状体であつて、長
さ方向に延伸されて全延伸倍率が3〜6倍となさ
れたポリエチレンテレフタレート樹脂製荷造りバ
ンド。 4 押出機の除湿機付乾燥ホツパーにて乾燥した
固有粘度(IV値)が0.90〜1.20のポリエチレンテ
レフタレートを金型より熔融押出し、この押出し
た熔融樹脂を第一水槽内で冷却して帯状体とし、
この帯状体を第一段延伸として85〜100℃の温度
で延伸倍率3〜4.5倍に延伸し、続いて第二段延
伸として250〜350℃の高温度で延伸して長さ方向
の全延伸倍率を4.6〜6倍とし、更に温度180〜
280℃の熱処理槽内をダウン率0〜5%の引取速
度で通過させて熱処理するポリエチレンテレフタ
レート樹脂製荷造りバンドの製造方法。[Scope of Claims] 1. A polyethylene terephthalate resin strip whose raw material has an intrinsic viscosity (IV value) of 0.90 to 1.20,
A packing band made of polyethylene terephthalate resin that is stretched in the length direction to have a total stretching ratio of 3 to 6 times. 2. A polyethylene terephthalate resin strip whose raw material has an inherent viscosity (IV value) of 0.90 to 1.20,
Packing made of polyethylene terephthalate resin, which is stretched in the length direction so that the total stretching ratio is 3 to 6 times, and furthermore, the molecular orientation arranged in the length direction over the entire range of the strip is disturbed by embossing. band. 3 A polyethylene terephthalate resin strip whose raw material has an intrinsic viscosity (IV value) of 0.90 to 1.20 and whose final molded product has an intrinsic viscosity (IV value) of 0.80 or more, which is stretched in the length direction to achieve a total stretching ratio of 0.90 to 1.20. A packing band made of polyethylene terephthalate resin that is 3 to 6 times larger. 4 Melt extrude polyethylene terephthalate with an intrinsic viscosity (IV value) of 0.90 to 1.20, dried in a drying hopper equipped with a dehumidifier of an extruder, from a mold, and cool the extruded molten resin in a first water tank to form a strip. ,
This strip-shaped body is stretched at a temperature of 85 to 100°C to a stretching ratio of 3 to 4.5 times as a first stage of stretching, and then stretched at a high temperature of 250 to 350°C as a second stage of stretching to fully stretch it in the length direction. The magnification is 4.6 to 6 times, and the temperature is 180 to
A method for manufacturing a packing band made of polyethylene terephthalate resin, which is heat-treated by passing it through a heat treatment tank at 280°C at a take-up speed with a down rate of 0 to 5%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14321380A JPS5768357A (en) | 1980-10-13 | 1980-10-13 | Packing band in polyethylene terephthalate resin and its manufacture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14321380A JPS5768357A (en) | 1980-10-13 | 1980-10-13 | Packing band in polyethylene terephthalate resin and its manufacture |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5768357A JPS5768357A (en) | 1982-04-26 |
| JPS6234624B2 true JPS6234624B2 (en) | 1987-07-28 |
Family
ID=15333511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14321380A Granted JPS5768357A (en) | 1980-10-13 | 1980-10-13 | Packing band in polyethylene terephthalate resin and its manufacture |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5768357A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59159319A (en) * | 1983-03-03 | 1984-09-08 | Mitsui Toatsu Chem Inc | Manufacture of uniaxially stretched polyester film |
| US4797313A (en) * | 1985-11-08 | 1989-01-10 | Monsanto Company | Non-metallic polymeric twist tie |
| JP2007008102A (en) * | 2005-07-04 | 2007-01-18 | Tanikawa Shoji Kk | Seal cap device |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5126113B1 (en) * | 1971-07-19 | 1976-08-04 | ||
| JPS5240667B2 (en) * | 1974-07-25 | 1977-10-13 | ||
| JPS51109063A (en) * | 1975-03-20 | 1976-09-27 | Tokumitsu Nakanose | Insatsuofushita netsukasoseigoseijushiseibandono seizohoho |
| JPS52108466A (en) * | 1976-03-08 | 1977-09-10 | Teijin Ltd | Method of manufacturing poly ethylene terephthalate film |
| IT1109831B (en) * | 1977-04-18 | 1985-12-23 | Signode Corp | FUSE COMPOSITE BINDING TIE |
| JPS5678942A (en) * | 1980-03-03 | 1981-06-29 | Sekisui Jushi Co Ltd | Preparation of band made of polyethylene terephthalate resin |
-
1980
- 1980-10-13 JP JP14321380A patent/JPS5768357A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5768357A (en) | 1982-04-26 |
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