JP3103042B2 - Antimicrobial PET resin master pellet and its composition - Google Patents
Antimicrobial PET resin master pellet and its compositionInfo
- Publication number
- JP3103042B2 JP3103042B2 JP09063728A JP6372897A JP3103042B2 JP 3103042 B2 JP3103042 B2 JP 3103042B2 JP 09063728 A JP09063728 A JP 09063728A JP 6372897 A JP6372897 A JP 6372897A JP 3103042 B2 JP3103042 B2 JP 3103042B2
- Authority
- JP
- Japan
- Prior art keywords
- pet resin
- melting point
- pet
- master pellet
- master
- 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 - Fee Related
Links
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- Apparatus For Disinfection Or Sterilisation (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Artificial Filaments (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、レギュラーポリエ
チレンテレフタレート(PET)樹脂原料から抗菌性の
PET製品を製造するための抗菌用PET樹脂マスター
ペレットに関する。TECHNICAL FIELD The present invention relates to an antibacterial PET resin master pellet for producing an antibacterial PET product from a regular polyethylene terephthalate (PET) resin raw material.
【0002】[0002]
【従来の技術】従来、PETに酸化チタン等の添加剤を
配合するには、先ず第一段階として添加剤を高濃度に含
有するマスターバッチ又はマスターペレットを製造して
おき、第二段階として原料PETに上記添加剤が所定濃
度になるようマスターペレットを添加して混合一体化す
るのが一般的であった。しかし、抗菌性のPET樹脂組
成物を製造するために、添加剤として銀ゼオライトを使
用する際に、銀ゼオライトを用いてマスターペレットを
製造しようとすると、銀ゼオライトの不均一分散のため
添加剤を均一混合するというマスターペレット本来の目
的達成が不可能であった。これを解決するため、銀ゼオ
ライトを予めポリオール系の溶剤に分散させておき、そ
の溶融スラリーをエキストルーダーでPET溶融物に混
入し、エキストルーダーで成形する、いわゆる”サイド
注入法”が提案されたが、この方法では一般的なマスタ
ーペレットを用いた場合に比して均一混合が困難であ
り、製品に品質むらを招き、製品価値の高いものが得ら
れなかった。また、各種製品の製造時に用いるエキスト
ルーダーも溶融スラリーの装置サイドから注入するため
に、特別の構造を必要とし、その結果、装置が高価なも
のとなり、さらに装置の汎用性がないので、少量生産や
製品切替えには大変であった。2. Description of the Related Art Conventionally, in order to mix an additive such as titanium oxide with PET, a master batch or a master pellet containing a high concentration of an additive is first manufactured in a first step, and a raw material is prepared in a second step. In general, a master pellet was added to PET so that the above additive had a predetermined concentration, followed by mixing and integration. However, when silver zeolite is used as an additive in order to produce an antimicrobial PET resin composition, when an attempt is made to produce master pellets using silver zeolite, the additive is used due to uneven dispersion of silver zeolite. It was impossible to achieve the original purpose of master pellets of uniform mixing. In order to solve this, a so-called "side injection method" has been proposed in which silver zeolite is dispersed in a polyol solvent in advance, and the molten slurry is mixed with a PET melt by an extruder and molded by an extruder. However, in this method, uniform mixing is more difficult than in the case of using general master pellets, resulting in uneven quality of the product, and a product having a high product value cannot be obtained. In addition, the extruder used in the manufacture of various products also requires a special structure to inject the molten slurry from the side of the equipment, resulting in expensive equipment and lack of versatility of the equipment. And it was hard to switch products.
【0003】[0003]
【発明が解決しようとする課題】10〜30重量%程度
の添加剤を含有するPETのマスターペレットは、一般
にPET樹脂に添加剤を混合し、加熱溶融後に、吐出口
金からうどん状に溶融PETを押出して連続的に水で冷
却する方法が採られている。これは溶融吐出後に水冷し
ないとなると、うどん状に吐出したPET樹脂の溶融物
が互いに融着して均一ペレットが得られないからであ
る。マスターペレットの添加剤として、銀ゼオライトを
用いる場合、水冷に使用する水が原因で、銀ゼオライト
結晶に結晶水のようにタイトに結合し、得られたマスタ
ーペレットを乾燥しても上記結晶水は除去されることが
なく、マスターペレットをレギラーPETペレットと混
合してエクストルーダーにより290〜300℃で溶融
吐出する段階に至って、始めて銀ゼオライトの結晶水が
放出される。この放出された水分の影響で、PETの解
重合が起き、物性低下を招き、例えばPET繊維を紡糸
する場合には、糸が切断して紡糸が困難となる不利があ
った。また、PET樹脂のフィルムや成形物を形成する
場合には、押出し後に白濁して透明感が失われ、厚みに
もばらつきを生じて良品ができないという問題点があっ
た。上記理由に鑑み、均一混合に適する銀ゼオライトの
PET樹脂マスターペレットを完成することにより、高
価な装置を用いることなく、スラリー法よりはるかに均
一混合が可能となり、汎用性のある簡便・有用な技術の
開発が渇望されていた。A master pellet of PET containing about 10 to 30% by weight of an additive is generally prepared by mixing an additive with a PET resin, melting it by heating, and then melting the PET into a udon shape from a discharge mouthpiece. And continuously cooling with water. This is because if water cooling is not performed after the melt-discharge, the melts of the PET resin discharged in a udon shape are fused to each other and uniform pellets cannot be obtained. When silver zeolite is used as an additive for the master pellets, the water used for water cooling causes the silver zeolites to bind tightly to the silver zeolite crystals like water of crystallization, and even if the obtained master pellet is dried, the water of crystallization remains Without being removed, the water of crystallization of silver zeolite is released for the first time until the master pellet is mixed with the Regillar PET pellet and melted and discharged at 290 to 300 ° C. by an extruder. Under the influence of the released water, depolymerization of PET occurs, resulting in a decrease in physical properties. For example, when spinning PET fibers, there is a disadvantage that the yarn is cut and spinning becomes difficult. In addition, when a PET resin film or molded product is formed, there is a problem that after extrusion, the film becomes cloudy and loses a sense of transparency, and the thickness also varies to make a non-defective product. In view of the above reasons, by completing PET resin master pellets of silver zeolite suitable for uniform mixing, it becomes possible to perform uniform mixing far more than the slurry method without using expensive equipment, and it is a versatile, simple and useful technology. The development of was craving.
【0004】[0004]
【課題を解決するための手段】従来のPETペレットで
は、290〜300℃で溶融されたPET樹脂の溶融物
は、押出機の口金から吐出されると、温度は低下するも
のの、ペレットにカットされる時点では未だ互いに融着
する温度を維持しているので、上記のようにどうしても
水冷工程が必要であった。本発明は、上記するように銀
ゼオライト含有のPET樹脂マスターペレットにおい
て、製造時の水冷工程を必要としない技術であり、本発
明で得られた銀ゼオライト含有のPET樹脂マスターペ
レットは、含まれる銀ゼオライトが全く結晶水を生成す
ることがないので、このPET樹脂マスターペレットを
混入したPET樹脂組成物の製造では従来のようなトラ
ブルの発生は全くないし、またこの組成物から製造され
た繊維及び成形品の品質に異常を与えることもない。す
なわち、本発明では、10〜30重量%の銀ゼオライト
を含有するPET樹脂マスターペレットを得るに当たっ
て、低融点のPET樹脂を使用し、含まれる水分調整を
実施することにより、レギュラーPET樹脂に混入した
とき、吐出後に水冷操作がなくとも吐出物同士の融着が
生じない成形物の得られることがわかった。In the conventional PET pellets, the molten PET resin melted at 290 to 300.degree. C. is cut into pellets, though the temperature is lowered when discharged from a die of an extruder. At a certain point, the temperature for fusing with each other is still maintained, so that a water cooling step was absolutely necessary as described above. The present invention is a technique that does not require a water-cooling step during production in a silver zeolite-containing PET resin master pellet as described above, and the silver zeolite-containing PET resin master pellet obtained in the present invention is a silver-containing zeolite-containing PET resin master pellet. Since the zeolite does not generate water of crystallization at all, the production of the PET resin composition mixed with the PET resin master pellets does not cause any trouble as in the prior art, and the fibers and moldings produced from this composition do not occur. There is no abnormality in product quality. That is, in the present invention, in obtaining a PET resin master pellet containing 10 to 30% by weight of silver zeolite, a low melting point PET resin was used, and the contained water was adjusted, whereby the PET resin was mixed into the regular PET resin. At this time, it was found that a molded product in which fusion of the discharged products did not occur without a water cooling operation after the discharge was obtained.
【0005】本発明では、150〜230℃の低融点の
PET樹脂を用いて、水冷しないでPET樹脂ペレット
を製造することにより水分含有量を400ppmにする
ことができた。230℃以上の融点のPET樹脂におい
ては、吐出後の水冷なしでは飴状の固まりとなり、ペレ
ットのカットができない。また、150℃以下の融点の
ペレットでは、低融点すぎてカット異常を招くのみなら
ず、レギュラーPETに混入すると混合物のPETの融
点低下がレギュラーPET樹脂本来の成形性を失うこと
になるので、本発明では150℃以下の低融点PET樹
脂は使用に適しない。PET樹脂は、通常、融点が25
0〜265℃程度のものが普通であるが、本発明では融
点が一般的なものより大幅に低い150〜230℃程度
のものを使用し、さらにマスターペレットとする際、そ
こに含まれる水分含有量を400ppm以下とすること
によって、レギュラーPETに混入したとき、吐出後に
水冷操作がなくとも吐出物同士の融着のないPET製品
が得られることが可能となった。[0005] In the present invention, a water content of 400 ppm could be obtained by producing PET resin pellets without cooling with water using a PET resin having a low melting point of 150 to 230 ° C. In the case of a PET resin having a melting point of 230 ° C. or higher, a candy-like mass is formed without water cooling after discharge, and pellets cannot be cut. In the case of pellets having a melting point of 150 ° C. or less, not only is the melting point too low, causing cut abnormalities, but also if mixed with regular PET, the melting point of the mixed PET decreases and loses the original moldability of regular PET resin. In the present invention, a low melting point PET resin having a temperature of 150 ° C. or lower is not suitable for use. PET resin usually has a melting point of 25.
The temperature is generally about 0 to 265 ° C, but in the present invention, a material having a melting point of about 150 to 230 ° C, which is much lower than a general melting point, is used. By setting the amount to 400 ppm or less, it becomes possible to obtain a PET product which is free from fusion of the ejected materials when it is mixed with regular PET without a water cooling operation after ejection.
【0006】本発明で得られるPET樹脂マスターペレ
ットと、キトサンとアジピン酸との反応生成物のキトサ
ン塩を併用することによりPET樹脂組成物の成形性を
より一層高めることができる。また、本発明に使用する
銀ゼオライトは、特に制限はなく、汎用の銀ゼオライト
が使用可能であるが、400℃程度の温度で焼成して無
水としたものが好ましい。本発明では、押出機からの溶
融吐出口でマスターバッチをカットし、マスターペレッ
トとしてペレットの包装封入までのわずかな時間大気に
触れることになるが、大気中の湿度の影響を受けても、
本発明のマスターペレットの水分含有量は400ppm
以下に管理することができるので、レギラーPET樹脂
に混合して繊維、フィルム、容器等の成型物を製造して
何ら異常がなく、透明性の喪失や厚みの不揃い、物性低
下などは全く生じない。本発明では、銀ゼオライトのマ
スターペレットは、例えば制電用のカチオン活性剤、キ
トサン、キトサン塩等、従来スラリー法に用いられてい
た化合物についても同様に使用できる。By using the PET resin master pellet obtained in the present invention in combination with the chitosan salt of the reaction product of chitosan and adipic acid, the moldability of the PET resin composition can be further enhanced. The silver zeolite used in the present invention is not particularly limited, and a general-purpose silver zeolite can be used. However, it is preferable that the zeolite is calcined at a temperature of about 400 ° C. to make it anhydrous. In the present invention, the master batch is cut at the melt discharge port from the extruder, and is exposed to the atmosphere for a short time until the packaging of the pellets as master pellets.
The water content of the master pellet of the present invention is 400 ppm
Since it can be managed as follows, it is mixed with Regular PET resin to produce molded products such as fibers, films, containers, etc., and there is no abnormality, loss of transparency, irregular thickness, no deterioration in physical properties, etc. . In the present invention, the master pellets of silver zeolite can be similarly used for compounds conventionally used in the slurry method, such as, for example, a cationic antistatic agent, chitosan, and chitosan salt.
【0007】[0007]
【実施例1】融点が220℃の低融点PET樹脂の品
名”RN−165”(商標名:日本ユニペット株式会社
製品)30重量部に、無水の銀ゼオライトとして”AK
−80H”(商標名:品川燃料株式会社製品)を10重
量部と、分散剤としてステアリン酸亜鉛0.5部を混合
して235℃で溶融し、押出機により2mmφのうどん
状に吐出し、水冷することなく長さ2mmにカットして
抗菌用PET樹脂マスターペレットを製造した。レギュ
ラーPET樹脂93重量部に上記抗菌用PET樹脂マス
ターペレット7部を混合してエクストルーダーにより2
90℃で溶融混合して40デニールで、20フイラメン
トの長繊維を何ら異常なく製造することができた。上記
長繊維を用いてトリコットによりハーフ生地を製編して
精錬仕上加工を行った。上記トリコット生地について、
SEKの菌数測定試験法にしたがって、大腸菌、黄色ブ
ドウ球菌、緑膿菌及びMRSAを植菌した結果、12時
間後でも菌が測定されなかった。得られたトリコット生
地は、抗菌効果が優れており、病院用として院内感染対
策用として十分使用することができる。Example 1 30 parts by weight of a low melting point PET resin having a melting point of 220 ° C. “RN-165” (trade name: manufactured by Nippon Unipet Co., Ltd.) were mixed with 30% by weight of “AK” as an anhydrous silver zeolite.
-80H "(trade name: Shinagawa Fuel Co., Ltd.), 10 parts by weight, and 0.5 part of zinc stearate as a dispersant were mixed and melted at 235 ° C., and extruded in an extruder into a 2 mmφ udon shape. The pellets were cut to 2 mm in length without water cooling to prepare PET resin master pellets for antibacterial use.93 parts by weight of regular PET resin were mixed with 7 parts of the above-mentioned master pellets for antimicrobial PET resin, and extruded.
At 40 denier after melt mixing at 90 ° C., 20 filament long fibers could be produced without any abnormality. A half dough was knitted by a tricot using the long fibers, and a refining finish was performed. About the above tricot dough,
As a result of inoculating Escherichia coli, Staphylococcus aureus, Pseudomonas aeruginosa and MRSA in accordance with the SEK count method, no bacteria were measured even after 12 hours. The obtained tricot dough has an excellent antibacterial effect, and can be sufficiently used for hospital use as a countermeasure for nosocomial infection.
【0008】[0008]
【実施例2】融点が190℃の低融点ポリエステル樹脂
45重量部に、無水の銀ゼオライトAK−80H(商品
名:品川燃料株式会社製品)を15重量部、キトサンと
アジピン酸を反応したキトサン塩を10重量部を混合し
て190℃で溶融し、押出機により2mmΦのうどん状
に吐出し、水冷することなく2mmにカットして抗菌用
PET樹脂マスターペレットを製造した。レギュラーP
ET樹脂95重量部に、実施例1に用いた抗菌用PET
樹脂マスターペレット5重量部を混合してエクストルー
ダーにより290℃で溶融混合してTダイより押出して
急速冷却して無延伸の厚さ200μmのシートとした。
得られたシートは、失透することなく透明で、均一な厚
さであった。SEKの菌数測定試験法にしたがって、大
腸菌、黄色ブドウ球菌及び緑膿菌を植菌したが、12時
間後にも菌は検出されず、抗菌効果の極めて優れたシー
トの得られていることが確認できた。Example 2 45 parts by weight of a low melting point polyester resin having a melting point of 190 ° C., 15 parts by weight of anhydrous silver zeolite AK-80H (product name: Shinagawa Fuel Co., Ltd.), and a chitosan salt obtained by reacting chitosan with adipic acid Was melted at 190 ° C., discharged in a 2 mmφ udon shape by an extruder, and cut into 2 mm without water cooling to produce an antimicrobial PET resin master pellet. Regular P
Antibacterial PET used in Example 1 was added to 95 parts by weight of ET resin.
Five parts by weight of the resin master pellets were mixed, melted and mixed at 290 ° C. by an extruder, extruded from a T-die, and rapidly cooled to obtain a non-stretched sheet having a thickness of 200 μm.
The obtained sheet was transparent without devitrification and had a uniform thickness. Escherichia coli, Staphylococcus aureus, and Pseudomonas aeruginosa were inoculated according to the SEK bacterial count test method, but no bacteria were detected even after 12 hours, and it was confirmed that a sheet with excellent antibacterial effect was obtained. did it.
【0009】[0009]
【実施例3】融点が160℃の低融点ポリエステル樹脂
40重量部に、無水の銀ゼオライトAK−80H(商品
名:品川燃料株式会社製品)10重量部を混合して19
0℃で溶融し、押出機により2mmΦのうどん状に吐出
し、水冷することなく2mmにカットして抗菌用PET
樹肥マスターペレットを製造した。レギュラーPET樹
脂95重量部に、実施例1に用いた抗菌用PET樹脂マ
スターペレット5重量部を混合して射出成型機を用いて
プリフォームを作り、室温まで冷却した。得られたプリ
フォームを加熱し、二軸延伸ブロー成型機で0.5mm
の厚さのストレッチブローボトルを製造した。成形後の
ボトルは、失透がなく、透明であった。得られたボトル
は、SEKの菌数測定試験法にしたがって、大腸菌、黄
色ブドウ球菌及び緑膿菌を植菌した結果、12時間後に
菌は測定されず、抗菌効果として優れたボトルであるこ
とがわかった。得られたボトルは、抗菌効果の優れてい
るので、水の保管用ボトルとして有用であった。Example 3 40 parts by weight of a low-melting polyester resin having a melting point of 160 ° C. and 10 parts by weight of anhydrous silver zeolite AK-80H (trade name: product of Shinagawa Fuel Co., Ltd.) were mixed and mixed.
Melt at 0 ° C, discharge into a 2mmφ udon shape with an extruder, cut to 2mm without water cooling and PET for antibacterial
Manure master pellets were produced. 95 parts by weight of the regular PET resin was mixed with 5 parts by weight of the antibacterial PET resin master pellet used in Example 1 to prepare a preform by using an injection molding machine, and cooled to room temperature. The obtained preform was heated, and 0.5 mm with a biaxial stretch blow molding machine.
Was manufactured. The bottle after molding was transparent without devitrification. The obtained bottle was inoculated with Escherichia coli, Staphylococcus aureus and Pseudomonas aeruginosa in accordance with the SEK bacteria count test method. As a result, no bacteria were measured after 12 hours, and the bottle was excellent in antibacterial effect. all right. The obtained bottle was excellent as an antibacterial effect, and thus was useful as a bottle for storing water.
【0010】[0010]
【発明の効果】本発明では、均一分散性の高い銀ゼオラ
イトのマスターペレットが得られるので、レギュラーP
ETと簡便に混入でき、高価な成形装置を用いることな
く、スラリー法よりはるかに均一混合が可能であり、得
られたPET製品の付加価値は高い。According to the present invention, a silver zeolite master pellet having a high uniform dispersibility can be obtained.
It can be easily mixed with ET, can be mixed far more uniformly than the slurry method without using expensive molding equipment, and the added value of the obtained PET product is high.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 中村 興司 大阪府大阪市東淀川区西淡路6丁目3番 41号 中村物産株式会社淡路工場内 (56)参考文献 特開 昭62−195037(JP,A) 特開 平8−113674(JP,A) (58)調査した分野(Int.Cl.7,DB名) C08J 3/22 C08L 67/00 - 67/02 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Koji Nakamura Inventor 6-41, Nishi-Awaji, Higashi-Yodogawa-ku, Osaka-shi, Osaka Inside the Awaji Plant of Nakamura Bussan Co., Ltd. (56) References JP-A-62-195037 (JP, A (58) Fields investigated (Int. Cl. 7 , DB name) C08J 3/22 C08L 67/00-67/02
Claims (3)
る融点150℃〜230℃の低融点ポリエチレンテレフ
タレ−ト樹脂を原料として、溶融吐出後に水で冷却する
ことなくペレットにされてなることを特徴とする水分含
有量が400 ppm以下の抗菌用ポリエチレンフタレ−ト樹
脂マスタ−ペレット。1. A low melting point polyethylene terephthalate resin having a melting point of 150.degree. C. to 230.degree. C. containing 10 to 30% by weight of silver zeolite as a raw material.
An antibacterial polyethylene phthalate resin master pellet having a water content of 400 ppm or less, characterized by being formed into pellets without being used.
なる250〜265℃の融点のポリエチレンテレフタレ
−ト樹脂組成物。2. A polyethylene terephthalate resin composition having a melting point of 250 to 265 ° C., comprising the master pellet of claim 1.
ンテレフタレ−ト樹脂に銀ゼオライトを10〜30重量
%含有せしめ、溶融吐出後に水で冷却することなくペレ
ット化することにより得られた水分含有量が400 ppm 以
下の抗菌用ポリエチレンテレフタレ−ト樹脂マスタ−ペ
レットを、融点250〜265℃のレギュラ−ポリエチ
レンテレフタレ−ト樹脂に配合することを特徴とするポ
リエチレンテレフタレ−ト樹脂成形品の製造方法。 3. A polyethylene having a low melting point of 150 ° C. to 230 ° C.
10-30 weight of silver zeolite in terephthalate resin
% After melting and discharging, without cooling with water.
The moisture content obtained by
Antibacterial polyethylene terephthalate resin master paper below
Lett is a regular polyethylene having a melting point of 250 to 265 ° C.
Characterized in that it is blended with lentephthalate resin.
A method for producing a polyethylene terephthalate resin molded product.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09063728A JP3103042B2 (en) | 1997-02-10 | 1997-02-10 | Antimicrobial PET resin master pellet and its composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09063728A JP3103042B2 (en) | 1997-02-10 | 1997-02-10 | Antimicrobial PET resin master pellet and its composition |
Publications (2)
Publication Number | Publication Date |
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JPH10219084A JPH10219084A (en) | 1998-08-18 |
JP3103042B2 true JP3103042B2 (en) | 2000-10-23 |
Family
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JP09063728A Expired - Fee Related JP3103042B2 (en) | 1997-02-10 | 1997-02-10 | Antimicrobial PET resin master pellet and its composition |
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JP (1) | JP3103042B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20180045420A (en) * | 2016-10-25 | 2018-05-04 | 한국생산기술연구원 | Manufacturing method of antibacterial materials using cation exchange reaction and antibacterial materials manufactured therefrom |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
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EP1449889B1 (en) * | 2001-10-17 | 2013-03-06 | Fuji Xerox Co., Ltd. | Antibacterial composite particles and antibacterial resin composition |
GB0410775D0 (en) * | 2004-05-14 | 2004-06-16 | Ineos Silicas Ltd | Masterbatch compositions |
JP2006233031A (en) * | 2005-02-25 | 2006-09-07 | Jsr Corp | Composition containing inorganic particle, transfer film and manufacturing method of plasma display panel |
JP4779106B1 (en) * | 2010-12-08 | 2011-09-28 | 憲司 中村 | Antibacterial water treatment agent |
KR101398909B1 (en) * | 2013-07-09 | 2014-05-27 | 주식회사히코 | Manufacturing of functional fiber with long lifetime |
CN111172614A (en) * | 2020-03-03 | 2020-05-19 | 百事基材料(青岛)股份有限公司 | Chitosan-containing polyester filament yarn and preparation method thereof |
CN114775097B (en) * | 2022-05-26 | 2023-05-23 | 青岛德冠超导材料制造有限公司 | Permanent antistatic antibacterial printable rinsing fiber and preparation method and application thereof |
-
1997
- 1997-02-10 JP JP09063728A patent/JP3103042B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20180045420A (en) * | 2016-10-25 | 2018-05-04 | 한국생산기술연구원 | Manufacturing method of antibacterial materials using cation exchange reaction and antibacterial materials manufactured therefrom |
Also Published As
Publication number | Publication date |
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JPH10219084A (en) | 1998-08-18 |
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