JPS58120657A - Non-rigid vinyl chloride resin film for agriculture - Google Patents

Non-rigid vinyl chloride resin film for agriculture

Info

Publication number
JPS58120657A
JPS58120657A JP57002257A JP225782A JPS58120657A JP S58120657 A JPS58120657 A JP S58120657A JP 57002257 A JP57002257 A JP 57002257A JP 225782 A JP225782 A JP 225782A JP S58120657 A JPS58120657 A JP S58120657A
Authority
JP
Japan
Prior art keywords
vinyl chloride
chloride resin
inert solid
fine particles
additive
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.)
Granted
Application number
JP57002257A
Other languages
Japanese (ja)
Other versions
JPS6230223B2 (en
Inventor
Hideo Umezawa
梅沢 英雄
Tamotsu Uejima
上島 保
Koichi Uchiki
内木 鋼一
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP57002257A priority Critical patent/JPS58120657A/en
Publication of JPS58120657A publication Critical patent/JPS58120657A/en
Publication of JPS6230223B2 publication Critical patent/JPS6230223B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/25Greenhouse technology, e.g. cooling systems therefor

Landscapes

  • Greenhouses (AREA)
  • Laminated Bodies (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:The titled film having improved transparency and low shrinkage, obtained by blending vinyl chloride resin with inert solid fine particles whose fine pores are filled with an additive for vinyl chloride resin, followed by making the blend into a film. CONSTITUTION:Fine pores of inert solid fine particles are previously filled with an additive for vinyl chloride resin until no occurrence of bubbles is observed when they are immersed in a polypropylene glycol bath heated at 160 deg.C, 100pts.wt. vinyl chloride resin is blended with 0.05-10pts.wt. inert solid fine particles, and made into a film. A plasticizer, a stabilizer, etc. is used as the additive for filling the fine pores, it is melted or dissolved in a solvent and processed into a solution, and it is blended with the inert solid fine particles by a mixer.

Description

【発明の詳細な説明】 本発明は、農業用軟質塩化ビニル樹脂フィルムに関し、
更に詳しくは透明性が良好で、かつ収縮が少ない不活性
固体微粒子を含む農業用軟質塩化ビニル樹脂フィルムに
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a soft vinyl chloride resin film for agricultural use,
More specifically, the present invention relates to an agricultural soft vinyl chloride resin film containing inert solid fine particles that has good transparency and little shrinkage.

近年、施設園芸においても、省エネルギーが大きく叫ば
れてきた結果、ビニールハウスの展張フィルムを2重、
3重に被覆(多重張シ)することにより、保温性を持た
せ、従来使用していた加温機を使わない方法へと変わり
つつある。
In recent years, energy conservation has become a big issue in greenhouse horticulture, and as a result, the expansion film for greenhouses has been double-layered,
Triple coating (multilayer coating) provides heat retention, and the method is changing to one that does not use the conventional heating device.

かかる展張用被覆フィルムとしては、軟質塩化ビニル樹
脂フィルムが圧倒的に広く使用されているが、軟質塩化
ビニル樹脂フィルムは高温時のペタツキが大きいため、
このように多重張り用に使用した場合、フィルム同志が
密着し易く、作業性が著しく悪い。そこで、この軟質塩
化ビニルフィルムの密着を少なくするために、種々の方
法が提案されており、中でも、炭酸カルシウム、クレー
、シリカ、タルク等の不活性固体微粒子を原料樹脂に練
シ込んで製膜する方法が効果が大きい。
Soft vinyl chloride resin films are overwhelmingly widely used as such stretching coating films, but since soft vinyl chloride resin films tend to flop at high temperatures,
When used in multiple layers in this manner, the films tend to stick together, resulting in extremely poor workability. Therefore, various methods have been proposed to reduce the adhesion of this soft vinyl chloride film. Among them, inert solid particles such as calcium carbonate, clay, silica, and talc are kneaded into the raw resin to form a film. This method is highly effective.

しかしながら、このような不活性固体微粒子を練り込ん
で製膜した軟質塩化ビニルフィルムは、(1)微細(直
径1 mlφ程度)な泡状の班点がフィルム全面わたっ
て大量に形成されやすく、(ii) 4た、ビニルハウ
スに展張時、大きく収縮するという欠点がある。
However, soft vinyl chloride films made by kneading such inert solid fine particles tend to (1) have a large amount of fine (about 1 mlφ in diameter) bubble-like spots formed over the entire surface of the film; ii) 4) Vinyl houses have the disadvantage of shrinking significantly when expanded.

(1)フィルム表面にかかる泡状の班点が多数存在する
と、透明性が損なわれ、有用な大陽光線の透過率が小さ
くなって栽培作物に悪影響を及ぼすし、(Il+ 4た
ビニールハウスに展張時大きく収縮すると、被覆が完全
に行なわれなくなるか破れるかするため、いずれも、農
業用フィルムとしては致命的な欠点となるものである。
(1) If there are many bubble-like spots on the film surface, the transparency will be impaired and the transmittance of the useful solar rays will be reduced, which will have a negative impact on cultivated crops. If the film shrinks significantly during stretching, the coating may not be completely applied or the film may be torn, both of which are fatal drawbacks for agricultural films.

本発明者らは、かかる点にかんがみて鋭意検討した結果
、上記不活性固体微粒子を含有するフィルム品質上の欠
点は、該不活性固体微粒子が多孔性であシ、細孔を有し
ていることに起因することを見出し、更に検討を進めた
結果、該不活性固体粒子の有する細孔空隙を軟質塩化ビ
ニル樹脂用添加剤で、あらかじめ充填した後、添加すれ
ば、上記欠点が解決されることも見出し、本発明を完成
した。
The inventors of the present invention have made extensive studies in view of the above points, and have found that the drawback in film quality containing the above-mentioned inert solid fine particles is that the inert solid fine particles are porous and have pores. As a result of further investigation, we found that the above drawbacks can be solved by filling the pore spaces of the inert solid particles with an additive for soft vinyl chloride resin before adding it. They also discovered this and completed the present invention.

すなわち、本発明に従って 不活性固体微粒子の有する細孔を、160℃に加熱した
ポリプロピレングリコール浴に浸漬した場合泡の発生が
ほぼ認められなくなるまで、あらかじめ塩化ビニル樹脂
用添加剤で充填した後、塩化ビニル樹脂に配合した樹脂
組成物を製膜してなる不活性固体微粒子含有農業用軟質
塩化ビニル樹脂フィルム。
That is, according to the present invention, the pores of the inert solid fine particles are filled with an additive for vinyl chloride resin until almost no bubbles are observed when immersed in a polypropylene glycol bath heated to 160°C, and then the pores are filled with an additive for vinyl chloride resin. A soft vinyl chloride resin film for agricultural use containing inert solid fine particles is formed by forming a film from a resin composition blended with vinyl resin.

が提供される。is provided.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明における不活性固体微粒子は01〜30μ程度の
粒径を有する無機質微粉末であって、たとえば、炭酸カ
ルシウム、炭酸マグネシウム、クレー(ケイ酸アルミニ
ウムの水和物)、シリカ、タルク(ケイ酸マグネシウム
の水和物)、ケイ酸カルシウム、二酸化チタン、硫酸バ
リウム等があげられる。これらは天然産の鉱物等をその
まま機械的に粉砕したものでもよいし、沈降法、熱分解
法、酸分解等により人工的に合成したものでもよい。
The inert solid fine particles in the present invention are inorganic fine particles having a particle size of about 0.01 to 30 μm, such as calcium carbonate, magnesium carbonate, clay (aluminum silicate hydrate), silica, talc (magnesium silicate), etc. hydrate), calcium silicate, titanium dioxide, barium sulfate, etc. These may be obtained by mechanically pulverizing naturally occurring minerals as they are, or may be artificially synthesized by a precipitation method, thermal decomposition method, acid decomposition method, or the like.

これらの不活性固体微粒子は塩化ビニル樹脂100重量
部当り 0.05〜10.0重量部程度、塩化ビニル樹
脂に添加され、他の塩化ビニル樹脂用添加剤と共に混合
される。
These inert solid fine particles are added to the vinyl chloride resin in an amount of about 0.05 to 10.0 parts by weight per 100 parts by weight of the vinyl chloride resin, and mixed with other additives for the vinyl chloride resin.

本発明においては、かかる不活性固体微粒子の有する細
孔を、塩化ビニル樹脂に添加する前に、あらかじめ塩化
ビニル樹脂用添加剤で充填する。
In the present invention, the pores of such inert solid fine particles are filled with an additive for vinyl chloride resin before adding them to the vinyl chloride resin.

この充填のための添加剤としては、たとえば、可塑剤、
安定剤、界面活性剤、滑剤等通常の軟質塩化ビニル樹脂
用添加剤がいずれも使用可能であシ、これらは、単独で
または2種以上複合して使用される。可塑剤としては、
たとえばモロ−オクチルフタレート、ジ(2−エチルヘ
キシル)フタレート、等のフタル酸誘導体やイソフタル
酸誘導体、ア゛ジピン酸誘導体、或いは、トリクレジル
ホスフェート、トリキシレニルホスフェート、等のリン
酸誘導体、各種エポキシ化合物等が挙げられる。安定剤
としては、ステアリン酸カルシウム、ステアリン酸バリ
ウム、ステアリン酸亜鉛、等の金属セッケン類や亜リン
酸エステル類等が挙げられる。界面活性剤としては、ン
ルビタンエステル、ジグリセリンエステル等ノニオン系
活性剤やイオン系活性剤等が挙げられる。滑剤としては
、ポリエチレンワックス、流動パラフィン、脂肪酸アミ
ド類等が挙げられる。
Additives for this filling include, for example, plasticizers,
Any of the usual additives for soft vinyl chloride resins such as stabilizers, surfactants, and lubricants can be used, and these may be used alone or in combination of two or more. As a plasticizer,
For example, phthalic acid derivatives such as moro-octyl phthalate and di(2-ethylhexyl) phthalate, isophthalic acid derivatives, adipic acid derivatives, phosphoric acid derivatives such as tricresyl phosphate and tricylenyl phosphate, various epoxy Examples include compounds. Examples of the stabilizer include metal soaps such as calcium stearate, barium stearate, zinc stearate, and phosphite esters. Examples of the surfactant include nonionic surfactants and ionic surfactants such as nrubitan ester and diglycerin ester. Examples of the lubricant include polyethylene wax, liquid paraffin, fatty acid amides, and the like.

不活性固体微粒子の有する細孔を上記軟質塩化ビニル樹
脂用添加剤で充填する方法は任意であるが、該固体微粒
子は樹脂用添加剤との親和性ないし濡れが良いので、固
体微粒子を液状の樹脂用添加剤と充分接触せしめるだけ
で、該細孔は添加剤で充填される。具体的には、該添加
剤を熔融せしめ、または他の溶剤に溶解して溶液とし、
要するに液状にしておいて、ヘンシェルミキサー、バン
バリーミキサ−、リボンプレンダー等通常のミキサーな
いしブレンダーを用いて不活性固体微粒子とブレンドす
ればよい。
Although the method of filling the pores of the inert solid fine particles with the above-mentioned additive for soft vinyl chloride resin is arbitrary, since the solid fine particles have good affinity or wettability with the resin additive, it is possible to fill the pores of the inert solid particles with the additive for the resin. Just enough contact with the resin additive fills the pores with the additive. Specifically, the additive is melted or dissolved in another solvent to form a solution,
In short, it can be made into a liquid and then blended with inert solid particles using a conventional mixer or blender such as a Henschel mixer, Banbury mixer, or ribbon blender.

この場合、使用する溶剤としては、該添加剤を溶かし、
塩化ビニル樹脂を溶かさないものが望ましく、たとえば
添加剤として界面活性剤であるソルビタンモノパルミテ
ートを使用する場合は、メタノール、エタノール、イソ
プロパツール、ベンゼン等があげられ、また、滑剤のメ
チレンビスステアロアミドを使用する場合は、ブタノー
ル、キシレン等があげられる。
In this case, the solvent used is one that dissolves the additive,
It is desirable to use something that does not dissolve the vinyl chloride resin. For example, when using the surfactant sorbitan monopalmitate as an additive, methanol, ethanol, isopropanol, benzene, etc. may be used, and the lubricant methylene bisstearate may be used. When using Roamide, butanol, xylene, etc. may be used.

充填温度は、添加剤を熔融状態で充填する場合は、その
融点以上の温度を適宜選択すればよく、通常20〜18
0℃が望ましい。また、溶液状態で充填する場合は、特
に温度的な制限はないが、通常は使用溶剤の沸点以下で
充填することが操作上好ましい。なお、溶液充填の場合
、使用溶剤が塩化ビニル樹脂に混入することが望ましく
ないものであるときは充填後、熱風乾燥、赤外線乾燥等
の手段で該溶剤を固体微粒子から蒸発せしめて除去する
必要がある。
When filling the additive in a molten state, the filling temperature may be appropriately selected at a temperature higher than the melting point of the additive, and is usually 20 to 18
0°C is desirable. Further, when filling in a solution state, there is no particular temperature restriction, but it is usually preferable for operation to fill at a temperature below the boiling point of the solvent used. In addition, in the case of solution filling, if it is undesirable for the solvent used to mix with the vinyl chloride resin, it is necessary to remove the solvent by evaporating it from the solid particles by hot air drying, infrared drying, etc. after filling. be.

また、充填に要する時間は、処理すべき不活性固体微粒
子の重量、樹脂用添加剤の種類、熔融状態で充填するか
溶液状態で充填するか、使用ミキサーの種類等によって
変シうるが、通常10分〜2時間程度である。
In addition, the time required for filling may vary depending on the weight of the inert solid particles to be treated, the type of resin additive, whether the filling is in a molten state or a solution state, the type of mixer used, etc., but normally It takes about 10 minutes to 2 hours.

本発明においては、上記のごとくして、不活性固体微粒
子の有する細孔を、あらかじめ塩化ビニル樹脂用添加剤
で充填するが、その充填の程度は、充填後の固体微粒子
を、「160℃に加熱したポリプロピレングリコール浴
に浸漬した場合、泡の発生がほとんど認められなくなる
まで」行うことが必要である。
In the present invention, as described above, the pores of the inert solid particles are filled in advance with an additive for vinyl chloride resin. When immersed in a heated polypropylene glycol bath, it is necessary to do so until the generation of bubbles is almost no longer observed.

ポリプロピレングリコール浴中で、発泡が認められる場
合は、固体微粒子の細孔がまだ十分に充填されていない
ことを示し、かかる固体微粒子を塩化ビニル樹脂に配合
してフィルムに製膜した場合、後記実施例に示すように
、フィルム表面に多数の泡状の班点が生成し、また、ビ
ニルノ・ウスに展張時大きく収縮する。
If foaming is observed in the polypropylene glycol bath, this indicates that the pores of the solid particles have not yet been sufficiently filled. As shown in the example, a large number of bubble-like specks are generated on the film surface, and the film also shrinks significantly when stretched on vinyl.

実際の操作においては、充填の途中で、ミキサーから、
適宜固体微粒子の小量を採取し、ポリプロピレングリコ
ール浴にて発泡状態をチェックしつつ、充填を行い、発
泡がほとんど認められなくなるまでブレンド操作を継続
すればよい。
In actual operation, during filling, from the mixer,
A small amount of solid fine particles may be appropriately collected, and filling may be performed while checking the foaming state in a polypropylene glycol bath, and the blending operation may be continued until foaming is hardly observed.

なお、発泡が認められなくなるまで不活性固体微粒子の
細孔を充填するに要する樹脂用添加剤の量は、該固体微
粒子の種類、細孔容量、細孔径、および見掛比重、等に
よって変シうるが、通常およそ不活性固体微粒子100
部当り10〜200重量部程度で十分である。もちろん
それ以上配合してもなんらさしつかえない。
The amount of resin additive required to fill the pores of the inert solid particles until foaming is no longer observed varies depending on the type, pore volume, pore diameter, apparent specific gravity, etc. of the solid particles. liquid, but usually about 100 inert solid particles
About 10 to 200 parts by weight per part is sufficient. Of course, there is nothing wrong with adding more than that.

本発明において用いられる塩化ビニル樹脂としては、塩
化ビニル単独重合体;塩化ビニルを主体とする他のビニ
ル単量体との共重合体、たとえば、酢酸ビニル、塩化ビ
ニリデン、マレイン酸ジエチル、エチレン、プロピレン
等との共重合体;これらのブレンド物;またはこれらと
他の重合体とのブレンド物が包含され、中でも塩化ビニ
ル重合体が好適である。
The vinyl chloride resin used in the present invention includes vinyl chloride homopolymers; copolymers mainly composed of vinyl chloride with other vinyl monomers, such as vinyl acetate, vinylidene chloride, diethyl maleate, ethylene, and propylene. copolymers with the like; blends thereof; and blends of these with other polymers, among which vinyl chloride polymers are preferred.

本発明のフィルムは、上記塩化ビニル樹脂に、前記のご
とくしてあらかじめ塩化ビニル樹脂用添加剤で細孔を充
填した不活性固体微粒子を配合し、さらに可塑剤、安定
剤、界面活性剤、滑剤等添加剤を加えて樹脂組成物とし
、これを公知の製膜方法、たとえば、熔融押出法、溶液
流延法、カレンダー法等によシ厚み30〜200μ程度
のフィルムに製造することによシ容易に得られる。
The film of the present invention is produced by blending inert solid fine particles whose pores are filled in advance with the vinyl chloride resin additive as described above into the vinyl chloride resin, and further including a plasticizer, a stabilizer, a surfactant, and a lubricant. A resin composition is prepared by adding additives such as the like, and is produced into a film with a thickness of about 30 to 200 μm by a known film forming method such as melt extrusion method, solution casting method, calender method, etc. easily obtained.

なお、本発明のフィルムには、添加剤として少くとも可
塑剤が含まれることが必須であり、塩化ビニル樹脂10
0部に対して、30〜60部程度が配合される。
In addition, it is essential that the film of the present invention contains at least a plasticizer as an additive, and vinyl chloride resin 10
About 30 to 60 parts are blended with respect to 0 parts.

次に実施例により本発明を説明する。Next, the present invention will be explained with reference to examples.

(実施例) (1)第1表に示した、不活性固体微粒子に、塩化ビニ
ル樹脂用添加剤を加えて、ヘンシェルミキサーでブレン
ドして細孔を充填した不活性固体微粒子C,E、Hを得
た。
(Example) (1) Inert solid fine particles C, E, H shown in Table 1 were added with an additive for vinyl chloride resin and blended in a Henschel mixer to fill the pores. I got it.

マタ、ソルビタンモノパルミテートをエタノールの20
%溶液とし、同様にヘンシェルミキサーで充填後201
ilIIgの減圧下50℃で20分間乾燥し固体微粒子
Fを得た。
Mata, 20% of sorbitan monopalmitate in ethanol
% solution and similarly filled with a Henschel mixer.
Solid fine particles F were obtained by drying at 50° C. for 20 minutes under reduced pressure of ilIIg.

これらは、いずれも、160℃に加熱したポリプロピレ
ングリコール浴に浸漬した場合、泡の発生がほとんど認
められないことを確認した。
It was confirmed that almost no bubbles were generated when these samples were immersed in a polypropylene glycol bath heated to 160°C.

(2)かくして得られた添加剤充填不活性固体微粒子を
第2表に示した添加量配合した下記組成物を得た。
(2) The following composition was obtained by adding the additive-filled inert solid fine particles thus obtained in the amounts shown in Table 2.

塩化ビニル樹脂(P=1300)    100部DO
P (ジオクチルフタレート)      50 〃エ
ポキシ樹脂           15〃ステアリン酸
バリウム       05〃〃   亜鉛     
    15〃(3)上記樹脂組成物を2本ロールで予
備混練した後、カレンダー法によ!+50μの厚さのフ
ィルムC′、E′、F′、H′を得た。
Vinyl chloride resin (P=1300) 100 parts DO
P (dioctyl phthalate) 50 Epoxy resin 15 Barium stearate 05 Zinc
15〃(3) After preliminary kneading the above resin composition with two rolls, use a calendar method! Films C', E', F', H' having a thickness of +50μ were obtained.

得られたフィルムについて、■泡状の班点数、■透明性
(かすみ度)、■収縮率、■密着度を測定した結果を第
2表に示す。
Table 2 shows the results of measuring the obtained film for (1) number of bubble-like spots, (2) transparency (degree of haze), (2) shrinkage rate, and (2) degree of adhesion.

(比較例) 塩化ビニル樹脂用添加剤でポリプロピレングリコール中
で泡の発生が認められる程度に充填を行った不活性固体
微粒子B、D、Gおよび全く充填を行わない微粒子Aを
使用したほかは実施例と同様の試験を行った結果金策1
表、および第2表に示す。
(Comparative example) Inert solid fine particles B, D, and G were filled with an additive for vinyl chloride resin to such an extent that bubble generation was observed in polypropylene glycol, and fine particles A were not filled at all. As a result of conducting the same test as in the example, money plan 1
Table 2.

以上、実施例、比較例から明らかなごとく、本発明によ
り提供される農業用軟質塩化ビニル樹脂フィルムは、多
重張シ等の際フィルム同志が密着することがないのはも
ちろん、(1)表面に泡状の班点がほとんど発生するこ
となく透明性が良好であり、また、(11)展張時に収
縮が少なく、農業分野に寄与するところ極めて犬である
As is clear from the above Examples and Comparative Examples, the agricultural soft vinyl chloride resin film provided by the present invention has the following advantages: It has good transparency with almost no foamy spots, and (11) has little shrinkage when expanded, making it extremely useful in the agricultural field.

なお、炭酸カルシウム等の不活性固体微粒子は、軽く容
易に飛散して粉塵となシやすいので、フィルムに練り込
む際、−面に固体微粒子のダストがまき上り、労働環境
衛生上も問題となっていたが、本発明の、細孔を樹脂用
添加剤で充填した不活性固体微粒子は、かかるダステン
グがほとんど生じないので環境衛生面上も望ましいもの
である。
In addition, inert solid fine particles such as calcium carbonate are light and easily scattered and become dust, so when they are kneaded into a film, the dust of solid fine particles is thrown up on the - side, which also poses a problem in terms of occupational health and environment. However, the inert solid fine particles of the present invention whose pores are filled with a resin additive are desirable from the viewpoint of environmental hygiene because such dusting hardly occurs.

特許出願人 三井東圧化学株式会社patent applicant Mitsui Toatsu Chemical Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] (1)不活性固体微粒子の有する細孔を、160℃に加
熱したポリプロピレングリコール浴に浸漬した場合泡の
発生がほとんど認められなくなるまで、あらかじめ塩化
ビニル樹脂用添加剤で充填した後、塩化ビニル樹脂に配
合した樹脂組成物を製膜してなる不活性固体微粒子含有
農業用軟質塩化ビニル樹脂フィルム。
(1) After filling the pores of the inert solid particles with an additive for vinyl chloride resin until almost no bubbles are observed when immersed in a polypropylene glycol bath heated to 160°C, An agricultural soft vinyl chloride resin film containing inert solid fine particles formed by forming a film from a resin composition blended with.
JP57002257A 1982-01-12 1982-01-12 Non-rigid vinyl chloride resin film for agriculture Granted JPS58120657A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57002257A JPS58120657A (en) 1982-01-12 1982-01-12 Non-rigid vinyl chloride resin film for agriculture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57002257A JPS58120657A (en) 1982-01-12 1982-01-12 Non-rigid vinyl chloride resin film for agriculture

Publications (2)

Publication Number Publication Date
JPS58120657A true JPS58120657A (en) 1983-07-18
JPS6230223B2 JPS6230223B2 (en) 1987-07-01

Family

ID=11524304

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57002257A Granted JPS58120657A (en) 1982-01-12 1982-01-12 Non-rigid vinyl chloride resin film for agriculture

Country Status (1)

Country Link
JP (1) JPS58120657A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50126053A (en) * 1974-03-25 1975-10-03
JPS5232899A (en) * 1975-09-10 1977-03-12 Hitachi Ltd Process for production of cubic boron nitride
JPS55164238A (en) * 1979-06-08 1980-12-20 Mitsubishi Petrochem Co Ltd Agricultural vinyl chloride resin film

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50126053A (en) * 1974-03-25 1975-10-03
JPS5232899A (en) * 1975-09-10 1977-03-12 Hitachi Ltd Process for production of cubic boron nitride
JPS55164238A (en) * 1979-06-08 1980-12-20 Mitsubishi Petrochem Co Ltd Agricultural vinyl chloride resin film

Also Published As

Publication number Publication date
JPS6230223B2 (en) 1987-07-01

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