JPS6342938B2 - - Google Patents

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Publication number
JPS6342938B2
JPS6342938B2 JP57093449A JP9344982A JPS6342938B2 JP S6342938 B2 JPS6342938 B2 JP S6342938B2 JP 57093449 A JP57093449 A JP 57093449A JP 9344982 A JP9344982 A JP 9344982A JP S6342938 B2 JPS6342938 B2 JP S6342938B2
Authority
JP
Japan
Prior art keywords
pvc
porosity
weight
matte
parts
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
JP57093449A
Other languages
Japanese (ja)
Other versions
JPS58210954A (en
Inventor
Hiromitsu Tachibana
Kazumasa Yamane
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry 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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP9344982A priority Critical patent/JPS58210954A/en
Publication of JPS58210954A publication Critical patent/JPS58210954A/en
Publication of JPS6342938B2 publication Critical patent/JPS6342938B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、良好な艶消し状態を有する成形体用
の塩化ビニル系樹脂組成物に関するものである。 最近、艶消し状成形体は高級感を有するため注
目を浴びている。かかる艶消し状成形体を得る方
法としては、従来から、加工時に機械的にいわゆ
るエンボス法で成形体表面に凹凸を付与する方法
が採用されていた。最近では、架橋剤モノマーに
よつて部分的に架橋した塩化ビニル樹脂(以下、
PVCという)を用いることによつて艶消し状成
形体を得る方法が提案されている。しかし、前者
の機械的方法では、エンボス用装置を設置する必
要があり、従つてコスト高になる上に、細かい艶
消し状成形体を得ることが困難である。また、後
者の架橋PVCを用いる方法では、架橋剤を用い
るためコスト高になることと、架橋剤のため成形
体の熱安定性が損なわれるという欠点がある。 本発明者等はかかる欠点を改良し、艶消し良好
なPVC系樹脂組成物に到達した。 即ち本発明は、(A)平均粒子径(直軽)が3〜
80μ、好ましくは5〜50μ、ポロシテイー(単位、
c.c./樹脂100g、以下同じ)が10以下、好ましく
は5以下のPVC10〜80重量部と(B)ポロシテイー
が15以上好ましくは20以上のPVC100重量部とか
らなるPVC系樹脂組成物を内容とする。 本発明でいうポロシテイー量は、樹脂100g当
り、水銀圧入式方法によつて求めた孔径0.17μ
(1000psi)〜5.9μ(20psi)のポロシテイー量(単
位、c.c./100gPVC)である。また、成形体の艶
消し状態は肉眼によつて観察した。 本発明を詳しく説明すると、艶消し状の成形体
品は、微小なゲル化不十分なPVC粒子を成形体
表面に存在さすことによつて目的を達成できる。
従つて加工成形時に、ゲル化速度が極端に異なる
樹脂を用いることによつて艶消し状の成形体を得
ることができる。次いで艶消し状態は、成形体表
面に存在する未ゲル化PVC粒子の大小により、
凹凸の大小が決定され、従つて艶消し状態も決定
される。 本発明において、(A)で用いるPVCはゲル化が
遅く、(B)で用いるPVCはゲル化が早い樹脂であ
る。(A)で用いるPVCの粒子径は成形体表面の凹
凸に関係があり、粒子径が小さい程、成形体の艶
消しの状態がきめ細かくなり、粒子径が大きい程
きめが粗くなる。但し粒子径が3μ未満となると
成形体の艶消し効果が得られなく、また粒子径が
80μをこえると艶消しというより異物が存在する
という感じを与える表面状態になるので好ましく
ない。好ましい粒子径は5〜50μがよい。また成
形体の艶消し状態は、(A)の使用量にも関係があ
り、少ないと艶消し効果はなく、また多すぎると
成形体の抗張力、伸びなどの物性が極端に低下す
るので好ましくない。好ましい使用量は10〜80重
量部の範囲が良い。次に(A)で用いるPVCのポロ
シテイーであるが、ポロシテイー量は小さい程、
ゲル化速度が遅くなる。(B)で用いるPVCとのゲ
ル化速度差を出し、艶消し状の成形体を得るに
は、暦(A)で用いるPVCのポロシテイーは10以下、
好ましくは5以下である。塩化ビニル樹脂のポロ
シテイーを制御する方法は種々知られているが、
最も一般的なのは2段重合法である。すなわち、
通常の塩化ビニルの重合度、更に塩化ビニルを追
加して重合するとポロシテイーは小さくなる。第
1段目モノマーの比率を小さくして第2段目モノ
マーの比率を大きくするほどポロシテイーは小さ
くなる。 (B)で用いるPVCは、ゲル化が早く、成形体品
では連続相を形成しているものである。この
PVCは一般の加工成形機で、通常の押出条件で
成形できる。この(B)のPVCとしては、ポロシテ
イーが15以上、好ましくは20以上が良い。通常一
般に市販されているPVCはこの範囲に入つてい
る。 本発明においては安定剤、滑剤、可塑剤、強化
剤、顔料、充填剤等PVC系樹脂の加工成形時用
いられる公知の成分を使用してよく、その使用量
も一般の量でよい。 尚、本発明の(A)及び(B)で用いるPVC中には、
塩化ビニルと共重合する他のモノマー成分が入つ
ていても何ら支障がない。但し、この場合塩化ビ
ニル成分が優位量(重量で)であるべきである。 以下に本発明の実施例を示すが、これらは何ら
本発明を限定するものでない。 参考例 撹拌翼を備えた内容積150の重合器に、イオ
ン交換水70Kg、部分ケン化ポリ酢酸ビニル25g、
ジメチルバレロニトリル20gを仕込み、脱気後、
塩化ビニル50Kg仕込み、65℃で所定時間重合し
た。次いで、塩化ビニルを所定量追加し、更に65
℃で所定時間重合し、ポロシテイーの異なるポリ
塩化ビニル(PVC)を得た。これらを次表に示
す。
The present invention relates to a vinyl chloride resin composition for molded articles having a good matte state. Recently, matte molded products have been attracting attention because of their luxurious appearance. Conventionally, as a method for obtaining such a matte molded body, a method has been adopted in which irregularities are mechanically imparted to the surface of the molded body by a so-called embossing method during processing. Recently, vinyl chloride resins (hereinafter referred to as
A method has been proposed to obtain a matte molded product by using PVC. However, in the former mechanical method, it is necessary to install an embossing device, which increases the cost and makes it difficult to obtain a fine matte molded product. Furthermore, the latter method using crosslinked PVC has the drawbacks of high cost due to the use of a crosslinking agent, and that the crosslinking agent impairs the thermal stability of the molded product. The present inventors have improved upon these drawbacks and achieved a PVC resin composition with good matte properties. That is, in the present invention, (A) the average particle diameter (direct light) is 3 to
80μ, preferably 5-50μ, porosity (unit,
(cc/100g of resin, hereinafter the same) is 10 to 80 parts by weight of PVC with a porosity of 10 or less, preferably 5 or less, and (B) 100 parts by weight of PVC with a porosity of 15 or more, preferably 20 or more. . The amount of porosity in the present invention is 0.17 μm in pore size determined by mercury intrusion method per 100 g of resin.
(1000psi) to 5.9μ (20psi) in cc/100g PVC. Further, the matte state of the molded product was observed with the naked eye. To explain the present invention in detail, the object of the matte molded article can be achieved by having minute PVC particles with insufficient gelation present on the surface of the molded article.
Therefore, by using resins with extremely different gelation rates during processing and molding, a matte molded product can be obtained. Next, the matte state depends on the size of the ungelled PVC particles present on the surface of the molded product.
The size of the unevenness is determined, and therefore the matte state is also determined. In the present invention, the PVC used in (A) is a resin that gels slowly, and the PVC used in (B) is a resin that gels quickly. The particle size of the PVC used in (A) is related to the unevenness of the surface of the molded object; the smaller the particle size, the finer the matte state of the molded object, and the larger the particle size, the coarser the texture. However, if the particle size is less than 3μ, the matting effect of the molded object cannot be obtained, and the particle size may be too small.
If the thickness exceeds 80μ, the surface condition will be more like the presence of foreign matter than matte, which is not preferable. The preferred particle size is 5 to 50μ. The matte state of the molded product is also related to the amount of (A) used; if it is too low, there will be no matting effect, and if it is too large, the physical properties such as tensile strength and elongation of the molded product will be extremely reduced, which is not desirable. . The preferred amount used is 10 to 80 parts by weight. Next, regarding the porosity of PVC used in (A), the smaller the porosity, the more
Gelation rate slows down. In order to create a gelling rate difference with the PVC used in (B) and obtain a matte molded product, the porosity of the PVC used in Calendar (A) should be 10 or less.
Preferably it is 5 or less. Various methods are known to control the porosity of vinyl chloride resin, but
The most common method is a two-stage polymerization method. That is,
When vinyl chloride is polymerized to a normal degree, and vinyl chloride is added to the polymer, the porosity becomes smaller. The smaller the ratio of the first-stage monomer and the larger the ratio of the second-stage monomer, the smaller the porosity becomes. The PVC used in (B) gels quickly and forms a continuous phase in the molded product. this
PVC can be molded using general processing and molding machines under normal extrusion conditions. The PVC (B) has a porosity of 15 or more, preferably 20 or more. Generally, commercially available PVC falls within this range. In the present invention, known components such as stabilizers, lubricants, plasticizers, reinforcing agents, pigments, fillers, etc. that are used during processing and molding of PVC resins may be used, and the amounts used may be in conventional amounts. In addition, in the PVC used in (A) and (B) of the present invention,
There is no problem even if other monomer components that copolymerize with vinyl chloride are included. However, in this case the vinyl chloride component should be the predominant amount (by weight). Examples of the present invention are shown below, but these are not intended to limit the present invention in any way. Reference example: In a polymerization vessel with an internal volume of 150 mm equipped with a stirring blade, 70 kg of ion-exchanged water, 25 g of partially saponified polyvinyl acetate,
After preparing 20g of dimethylvaleronitrile and degassing,
50 kg of vinyl chloride was charged and polymerized at 65°C for a predetermined time. Next, add a predetermined amount of vinyl chloride, and add 65
Polyvinyl chloride (PVC) with different porosity was obtained by polymerization at ℃ for a predetermined period of time. These are shown in the table below.

【表】 実施例1〜5、参照例1、比較例1 平均重合度1000、ポロシテイー20.5、平均粒子
径130μのPVC(B樹脂)100重量部に平均重合度
700で、平均粒子径及びポロシテイーが異なる
PVC(A樹脂)50重量部及びスズ系安定剤3重量
部、低分子量ポリエチレン0.7重量部からなる混
合物から50mm押出機で厚さ0.7mmのシートを作り、
その艶消し状態を観察した。その結果を表1に示
す。
[Table] Examples 1 to 5, Reference Example 1, Comparative Example 1 Average degree of polymerization to 100 parts by weight of PVC (B resin) with average degree of polymerization 1000, porosity 20.5, and average particle size 130μ
700 with different average particle size and porosity
A sheet with a thickness of 0.7 mm was made using a 50 mm extruder from a mixture consisting of 50 parts by weight of PVC (Resin A), 3 parts by weight of a tin-based stabilizer, and 0.7 parts by weight of low molecular weight polyethylene.
The matte state was observed. The results are shown in Table 1.

【表】 表1から、艶消し状態の良いPVCはポロシテ
イー10以下、好ましくは5以下、平均粒子径が3
〜80μ、好ましくは5〜50μであることが判る。 実施例6〜10、参照例2、比較例2 平均重合度1300、ポロシテイー26、平均粒子径
130μのPVC(B樹脂)100重量部に、平均重合度
750、ポロシテイーが3で、平均粒子径の異なる
PVC(A樹脂)40重量部、ステアリン酸鉛1.5重量
部、ステアリン酸カルシウム0.5重量部、ジ―2
―エチルヘキシルフタレート70重量部及びカーボ
ンブラツク0.02重量部からなる配合物から、40mm
押出機で径5mmの円形状の押し出し物を作製し、
その表面の艶消し状態を観察した結果を表2に示
す。
[Table] From Table 1, PVC with good matte condition has a porosity of 10 or less, preferably 5 or less, and an average particle size of 3.
~80μ, preferably 5-50μ. Examples 6 to 10, Reference Example 2, Comparative Example 2 Average degree of polymerization 1300, porosity 26, average particle diameter
100 parts by weight of 130μ PVC (B resin), average degree of polymerization
750, the porosity is 3 and the average particle size is different.
PVC (A resin) 40 parts by weight, lead stearate 1.5 parts by weight, calcium stearate 0.5 parts by weight, G-2
- 40 mm from a blend of 70 parts by weight of ethylhexyl phthalate and 0.02 parts by weight of carbon black
Create a circular extrudate with a diameter of 5 mm using an extruder,
Table 2 shows the results of observing the matte state of the surface.

【表】 * A樹脂を用いていない。
** 艶消し状態のランクは表1に同じ。
表2から、軟質系の場合にも、本発明に従えば
艶消し効果の良い成形体が得られることが判る。 実施例11〜14、参照例3、比較例3 平均重合度680、ポロシテイー20、平均粒子径
150μのPVC(B)100重量部に、平均重合度680、ポ
ロシテイー4、平均粒子径15μのPVC(A)、カネエ
ースB―22(鐘淵化学工業(株)製)10重量部、スズ
系安定剤3重量部、エステル系ワツクス0.8重量
部、及びブルー系顔料0.005重量部からなる配合
物から、50mmブローボトル成形機でボトルを成形
し、成形体の艶消し状態を観察した。その結果を
表3に示す。
[Table] *A resin is not used.
** Ranks for matte condition are the same as in Table 1.
From Table 2, it can be seen that even in the case of a soft type, a molded article with good matting effect can be obtained according to the present invention. Examples 11 to 14, Reference Example 3, Comparative Example 3 Average degree of polymerization 680, porosity 20, average particle size
100 parts by weight of PVC (B) of 150 μ, PVC (A) with an average degree of polymerization of 680, porosity of 4, average particle size of 15 μ, 10 parts by weight of Kane Ace B-22 (manufactured by Kanebuchi Kagaku Kogyo Co., Ltd.), tin-based stable A bottle was molded using a 50 mm blow bottle molding machine from a blend consisting of 3 parts by weight of agent, 0.8 part by weight of ester wax, and 0.005 part by weight of blue pigment, and the matte state of the molded product was observed. The results are shown in Table 3.

【表】 * 艶消し状態のランクは表1に同じ。
表3から成形体の艶消し状態は樹脂(A)の使用量
によつて変わることが判る。
[Table] * The rank of matte condition is the same as in Table 1.
Table 3 shows that the matte state of the molded article changes depending on the amount of resin (A) used.

Claims (1)

【特許請求の範囲】 1 (A)平均粒子径が3〜80μ、ポロシテイー(単
位、c.c./樹脂100g)が10以下の塩化ビニル樹脂
10〜80重量部、(B)ポロシテイーが15以上の塩化ビ
ニル樹脂100重量部とからなる塩化ビニル系樹脂
組成物。 2 特許請求の範囲第1項において、(A)なる塩化
ビニル系樹脂の平均粒子径が5〜50μ、ポロシテ
イーが5以下である塩化ビニル系樹脂組成物。
[Scope of Claims] 1 (A) A vinyl chloride resin with an average particle diameter of 3 to 80μ and a porosity (unit, cc/100g of resin) of 10 or less
10 to 80 parts by weight, and (B) 100 parts by weight of a vinyl chloride resin having a porosity of 15 or more. 2. The vinyl chloride resin composition according to claim 1, wherein the vinyl chloride resin (A) has an average particle diameter of 5 to 50 μm and a porosity of 5 or less.
JP9344982A 1982-05-31 1982-05-31 Good delustered vinyl chloride resin composition Granted JPS58210954A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9344982A JPS58210954A (en) 1982-05-31 1982-05-31 Good delustered vinyl chloride resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9344982A JPS58210954A (en) 1982-05-31 1982-05-31 Good delustered vinyl chloride resin composition

Publications (2)

Publication Number Publication Date
JPS58210954A JPS58210954A (en) 1983-12-08
JPS6342938B2 true JPS6342938B2 (en) 1988-08-26

Family

ID=14082630

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9344982A Granted JPS58210954A (en) 1982-05-31 1982-05-31 Good delustered vinyl chloride resin composition

Country Status (1)

Country Link
JP (1) JPS58210954A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62285938A (en) * 1986-06-04 1987-12-11 Toyoda Gosei Co Ltd Automobile side molding

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5692024A (en) * 1979-12-27 1981-07-25 Mitsubishi Monsanto Chem Co Preparation of vinyl chloride resin film
JPS56106945A (en) * 1980-01-29 1981-08-25 Chisso Corp Vinyl chloride resin composition for fluidized bed dip coating

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5692024A (en) * 1979-12-27 1981-07-25 Mitsubishi Monsanto Chem Co Preparation of vinyl chloride resin film
JPS56106945A (en) * 1980-01-29 1981-08-25 Chisso Corp Vinyl chloride resin composition for fluidized bed dip coating

Also Published As

Publication number Publication date
JPS58210954A (en) 1983-12-08

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