JPS63175057A - Vinyl chloride based polymer composition - Google Patents

Vinyl chloride based polymer composition

Info

Publication number
JPS63175057A
JPS63175057A JP557287A JP557287A JPS63175057A JP S63175057 A JPS63175057 A JP S63175057A JP 557287 A JP557287 A JP 557287A JP 557287 A JP557287 A JP 557287A JP S63175057 A JPS63175057 A JP S63175057A
Authority
JP
Japan
Prior art keywords
vinyl chloride
polymerization
polymer composition
chloride polymer
based polymer
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
JP557287A
Other languages
Japanese (ja)
Other versions
JPH0547581B2 (en
Inventor
Naoyoshi Kimura
直悦 木村
Yasuo Murase
村瀬 康夫
Kazuya Aso
阿曾 一也
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.)
Mitsubishi Kasei Vinyl Co
Original Assignee
Mitsubishi Kasei Vinyl Co
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 Mitsubishi Kasei Vinyl Co filed Critical Mitsubishi Kasei Vinyl Co
Priority to JP557287A priority Critical patent/JPS63175057A/en
Publication of JPS63175057A publication Critical patent/JPS63175057A/en
Publication of JPH0547581B2 publication Critical patent/JPH0547581B2/ja
Granted legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain a vinyl chloride based polymer composition capable of providing a low-viscosity plastisol, by containing a specific phosphoric acid ester based compound in a vinyl chloride based polymer. CONSTITUTION:A composition obtained by adding and dispersing (A) phosphoric acid esters (blend) expressed by formula I (R is 8-30C alkyl or alkylphenyl; k is 1-3; l and m is 0-2 and k+l+m=3; M is alkali metal or ammonium group; n is 0-15), preferably a blend of the ester in which R is nonylphenyl; m=0; n=9; k=1 and l=2 with the ester in which k=2 and l=1 at 1:4-4:1 blending ratio of the former to the latter in an amount within the range of 0.1-5pts.wt., preferably 0.3-3pts.wt. in (B) 100pts.wt. polymerized latex of a vinyl chloride based polymer, preferably obtained by emulsion polymerization or finely suspension polymerization using an alkyl phenyl ether sulfonate as an emulsifying agent and spray drying the resultant blend.

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、低粘度のプラスチゾルを与えることの出来る
塩化ビニル系重合体組成物に係わる。
DETAILED DESCRIPTION OF THE INVENTION "Industrial Application Field" The present invention relates to a vinyl chloride polymer composition capable of providing a plastisol with low viscosity.

「従来の技術」 ペースト用塩化ビニル系重合体は、通常水溶性の重合開
始剤を用いた乳化重合法または塩化ビニル単量体に溶解
するいわゆる油溶性重合開始剤を用い、塩化ビニル単量
体を機械的に水中に均一かつ微細に分散させた(均質化
処理した)a重合する微細懸濁重合法によって91遺さ
れている。このとき、乳化剤として高級アルコール硫酸
エステル塩、アルキルスルホン酸塩、アル斗ルアリール
スルホン酸塩のような陰イオン界面活性剤が主に使用さ
れている。このようにして得られたペースト用塩化ビニ
ル系重合体は、例えば重合体に可塑剤、希釈胴、安定剤
等を配合して調製したプラスチゾル、オルガノゾル等の
ペースト分散液の粘度が高く、成形加工が困難になると
いう大きな欠点があった。
``Prior art'' Vinyl chloride polymers for paste are usually produced by emulsion polymerization using a water-soluble polymerization initiator or by using a so-called oil-soluble polymerization initiator that dissolves in vinyl chloride monomer. 91 were carried out by a micro-suspension polymerization method in which a polymer is mechanically and uniformly and finely dispersed (homogenized) in water. At this time, anionic surfactants such as higher alcohol sulfate salts, alkyl sulfonate salts, and arylaryl sulfonate salts are mainly used as emulsifiers. The vinyl chloride polymer for paste obtained in this way has a high viscosity as a paste dispersion such as plastisol or organosol prepared by blending the polymer with a plasticizer, a diluent, a stabilizer, etc., and is difficult to mold. The major drawback was that it was difficult to

しかして、ゾル粘度を低下する等の目的で、重合後のラ
テックスに上述の陰イオン界面活性剤やポリオキシエチ
レンアルキルエーテル、ポリオキンエチレンポリオキシ
ブロビレンブロック共重合物、ソルビタンエステル、グ
リセリンアルキルエステルなどの非イオン界面活性剤の
1種または2種以上を適宜量加えて乾燥するペースト用
塩化ビニル系重合体のg1造方法や、またはゾル調製時
に一ヒ述した界面活性剤を加えることも行われている。
Therefore, for the purpose of reducing sol viscosity, the above-mentioned anionic surfactants, polyoxyethylene alkyl ether, polyoxyethylene polyoxybrobylene block copolymer, sorbitan ester, glycerin alkyl ester are added to the latex after polymerization. It is also possible to use the g1 manufacturing method of vinyl chloride polymer for paste, which involves adding an appropriate amount of one or more nonionic surfactants such as, and drying, or adding the surfactants mentioned above at the time of sol preparation. It is being said.

しかし、この様な一般的な方法では粘度低下の点で必ず
しも十分な結果は得られていない。
However, such general methods do not always yield sufficient results in terms of viscosity reduction.

[発明が解決しようとする問題点」 本発明者らは、上述のような従来の欠点のない低粘度の
プラスチゾルを与える塩化ビニル系重合体組成物につい
て検討をおこなっており、既に、特定の陰イオン系界面
活性剤を重合の際の乳化剤として用いたり、或は、重合
後のilNlN乳用乳化剤て用いる等により低粘度でか
つ粘度安定性、熱安定性の良好なプラスチゾルが得られ
ることを見出している(特願昭59−1.67331、
特願昭59−167332)、この効果を更に高め、よ
り低粘度のプラスチゾルを与える塩化ビニル系重合体組
成物について検討を実施した結果、塩化ビニル系重合体
に特定の燐酸エステル系化合物を含有させることにより
、本発明の目的を達成しうろことを発見し本発明を完成
するに至った。
[Problems to be Solved by the Invention] The present inventors have been studying a vinyl chloride polymer composition that provides a low-viscosity plastisol without the above-mentioned conventional drawbacks, and have already found certain problems. It was discovered that a plastisol with low viscosity and good viscosity stability and thermal stability can be obtained by using an ionic surfactant as an emulsifier during polymerization or as an emulsifier for ilNlN milk after polymerization. (Patent application 1986-1.67331,
(Japanese Patent Application No. 59-167332), as a result of research into a vinyl chloride polymer composition that further enhances this effect and provides plastisol with a lower viscosity, it was discovered that a specific phosphoric acid ester compound was incorporated into the vinyl chloride polymer. As a result, the inventors discovered that the object of the present invention could be achieved and completed the present invention.

すなわち、本発明の目的は、粘度が低いプラスチゾルを
与えることのできる塩化ビニル系重合体組成物を提供す
るにある。
That is, an object of the present invention is to provide a vinyl chloride polymer composition that can provide plastisol with low viscosity.

「問題点を解決するための手段、1 しかして、本発明の要旨とするところは、塩化ビニル系
重合体100重量部に、一般式[[]%式%() (式中、Rは炭素数8から30のアルキル基またはアル
キルフェニル基 には1から3の整数、1および論は0から2の整数で、
k+1十−二3、 Mはアルカリ−&属原子、 またはアンモニウム基、 nはOから15の整数 をそれぞれ示す。) で−&される燐酸エステルまたはその混合物を0.1〜
5重量部含有せしめた塩化ビニル系重合体組成物に存す
る。
``Means for Solving the Problems, 1'' However, the gist of the present invention is to add 100 parts by weight of a vinyl chloride polymer with the general formula [[]% formula %() (wherein R is carbon The alkyl group or alkylphenyl group of numbers 8 to 30 is an integer of 1 to 3, 1 and 2 are integers of 0 to 2,
k+10-23, M is an alkali atom or an ammonium group, and n is an integer from O to 15, respectively. ) phosphoric acid ester or mixture thereof
5 parts by weight of the vinyl chloride polymer composition.

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

本発明の組成物に用いる塩化ビニル系重合体とは、塩化
ビニル単量体または塩化ビニルとこれに共重合可能な他
の単量体、例えば、エチレン、プロピレン、n−ブテン
のようなオレフィン類、酢酸ビニル、プロピオン酸ビニ
ル、ステアリン酸ビニルのようなビニルエステル、アク
リル酸、メタクリル酸、イタコン酸のような不飽和酸ま
たはそれらのアルキルエステル、メチルビニルエーテル
、エチルビニルエーテル、オクチルビニルエーテル、ラ
ウリルビニルエーテルのようなビニルエーテル、マレイ
ン酸、7マル酸あるいはこれらの無水物またはエステル
、芳香族ビニル化合物、不飽和ニトリル等の単量体の1
種又は2種以上との共重合体が挙げられる。塩化ビニル
と共重合可能な単量体は、上述のものに限定されるもの
ではなく、また共重合体の場合、共重合可能な単量体の
含有量は、共重合体の30重量%以下、好ましくは2O
重量%以下の範囲であるのが望ましい。また本発明にお
いて用いる塩化ビニル系重合体の!!遣方法は、乳化重
合法または微m懸濁重合法によるが、その時に使用する
乳化剤が特に下記、一般式[rll(式中、R5は炭素
数6〜18のアルキル基、pはθ〜4の整数、 Xは−CH2−CH−CH,−または H −cH2−CHt−で示される基 Mはアルカリ*属原子またはアンモニウム基、 をそれぞれ示す、) で表されるアルキルフェニルエーテルのスルホネ−F塩
であるのが好ましい。
The vinyl chloride polymer used in the composition of the present invention refers to vinyl chloride monomer or vinyl chloride and other monomers copolymerizable therewith, such as olefins such as ethylene, propylene, and n-butene. , vinyl esters such as vinyl acetate, vinyl propionate, vinyl stearate, unsaturated acids such as acrylic acid, methacrylic acid, itaconic acid or their alkyl esters, such as methyl vinyl ether, ethyl vinyl ether, octyl vinyl ether, lauryl vinyl ether One of the monomers such as vinyl ether, maleic acid, 7-malic acid or anhydride or ester thereof, aromatic vinyl compound, unsaturated nitrile, etc.
Examples include species or copolymers with two or more species. Monomers copolymerizable with vinyl chloride are not limited to those mentioned above, and in the case of a copolymer, the content of monomers copolymerizable with vinyl chloride is 30% by weight or less of the copolymer. , preferably 2O
It is desirable that the amount is within the range of % by weight or less. Also, the vinyl chloride polymer used in the present invention! ! The method of polymerization is emulsion polymerization method or fine suspension polymerization method, and the emulsifier used at that time is particularly represented by the following general formula [rll (wherein R5 is an alkyl group having 6 to 18 carbon atoms, p is θ to 4 Sulfone-F of an alkylphenyl ether represented by Preferably it is salt.

なかでも上記一般式[IT]で表されるアルキル7エ二
ルエーテルのスルホネート塩がp−オクチルフェニルジ
オキシエチレン−3−スルホ−2−ヒドロキシプロピル
エーテルのアルカリ金属塩またはアンモニウム塩、もし
くは、p−才クチルフェニルジオキシ−エチレン−2−
スルホエチルエーテルのアルカリ金属塩またはアンモニ
ウム塩であるのが最も好ましい。
Among them, the sulfonate salt of alkyl 7 enyl ether represented by the above general formula [IT] is the alkali metal salt or ammonium salt of p-octylphenyldioxyethylene-3-sulfo-2-hydroxypropyl ether, or the p- Cutylphenyldioxy-ethylene-2-
Most preferred are the alkali metal or ammonium salts of sulfoethyl ether.

本発明の組成物の一成分である一般式[I]で表される
燐酸エステルは、式中のRは炭素数8〜30のアルキル
基またはアルキル7ヱニル基であり、待にアルキルフェ
ニル基が好ましい。
In the phosphoric acid ester represented by the general formula [I] which is a component of the composition of the present invention, R in the formula is an alkyl group having 8 to 30 carbon atoms or an alkyl 7enyl group, and an alkylphenyl group is present. preferable.

kは1から3の整数であり、I、mはそれぞれθ〜2の
整数であって、k+l+m=3を満足する必要があるが
、kは1または2、−はOであるのが好ましい。nはO
〜15の整数であり、特に3〜10の範囲にあるのが好
ましい。
k is an integer from 1 to 3, I and m are each integers from θ to 2, and it is necessary to satisfy k+l+m=3, but preferably k is 1 or 2, and - is O. n is O
It is an integer of 15 to 15, preferably in the range of 3 to 10.

該燐酸エステルを混合物として用いる場合、陽=0で、
k=、1のものとに=2のものを混合するのが好ましい
が、その混合比は、k=1:に=2で示す時1:9〜9
:1、特に、1:4〜4:1の範囲にあるのが好ましい
When the phosphoric acid ester is used as a mixture, positive = 0,
It is preferable to mix k = 1 with k = 2, but the mixing ratio is 1:9 to 9 when k = 1: to = 2.
:1, particularly preferably in the range of 1:4 to 4:1.

該燐酸エステルまたはその混合物は、例えハ燐酸のモノ
、及びジ(アルキルフェニルポリオキシエチレン)エス
テル、もしくはそれらのアルカリ金属塩またはアンモニ
ウム塩が挙げられる6該燻酸エステル(混合物)は、塩
化ビニル系重合体100重量部に対して、O−1〜5重
量部、好ましくは0.3〜3重量部の範囲で含有されて
いるのが望ましい。
Examples of the phosphoric acid ester or mixture thereof include mono- and di(alkylphenylpolyoxyethylene) esters of phosphoric acid, or alkali metal salts or ammonium salts thereof.6 The smoking acid ester (mixture) is a vinyl chloride-based ester. It is desirable that the content is in the range of 1 to 5 parts by weight, preferably 0.3 to 3 parts by weight, per 100 parts by weight of the polymer.

塩化ビニル系重合体に一般式[I]で表される燐酸エス
テルまたはその混合物を含有せしめるには、例えば次の
各種方法が採用される。
In order to incorporate the phosphoric acid ester represented by the general formula [I] or a mixture thereof into the vinyl chloride polymer, the following various methods are employed, for example.

■ 乳化重合または微細懸濁重合時に、該燐酸エステル
を、乳化剤または補助乳化剤として存在せしめ、得られ
た塩化ビニル系重合体ラテックスをそのまま噴霧乾燥す
る。
(2) The phosphoric acid ester is made to exist as an emulsifier or an auxiliary emulsifier during emulsion polymerization or fine suspension polymerization, and the resulting vinyl chloride polymer latex is directly spray-dried.

■ 乳化重合または微細懸濁重合して得られた塩化ビニ
ル系重合体ラテックスに、該燐酸ニスチルを調整用乳化
剤として添加して、そのラテックスを噴霧乾燥する。
(2) The nistyl phosphate is added as a controlling emulsifier to a vinyl chloride polymer latex obtained by emulsion polymerization or fine suspension polymerization, and the latex is spray-dried.

■ 乳化重合または微#I患濁重合して得られた塩化ビ
ニル系重合体から可塑剤、安定剤等を添加してプラスチ
ゾルを調製する際に、該燐酸エステル(混合物)を、添
加する。
(2) The phosphoric acid ester (mixture) is added when plastisol is prepared by adding a plasticizer, stabilizer, etc. from a vinyl chloride polymer obtained by emulsion polymerization or fine #I turbidity polymerization.

勿論、塩化ビニル系重合体に燐酸エステル(混合物)を
含有せしめる方法は、上述の方法だけに限定されるもの
ではなく、各種の方法が採用され得るが、本発明の組成
物では上述の■または■の方法によって調91されたも
のが好ましく、待に■のように乳化重合または微#I患
濁重合した塩化ビニル系重合体ラテックスに、燐酸エス
テル(混合物)を添加したものを噴霧乾燥したものが、
組成物の製造ヒまたゾルの調整上好ましい態様である。
Of course, the method of incorporating the phosphoric acid ester (mixture) into the vinyl chloride polymer is not limited to the above-mentioned method, and various methods may be adopted. Preferably, it is prepared by the method (2), which is prepared by spray-drying a vinyl chloride polymer latex that has been subjected to emulsion polymerization or slight #I turbidity polymerization as in (2), to which a phosphoric acid ester (mixture) is added. but,
This is a preferred embodiment for the preparation of the composition and for the preparation of the sol.

「発明の効果」 本発明の組成物からllI整されたプラスチゾルの粘度
は、低剪断速度領域のみならず、高剪断速度領域におい
ても低い値を示し、プラスチゾルの流動性に優れ、この
効果は塗布法によるプラスチゾルの加工分野において特
に有利である。例えば、低剪断速度範囲におけるゾル粘
度が低いため、ペーストゾルの取扱い、例えば供給、ろ
過、脱泡が容易となり、また高剪断速度範囲におけるゾ
ル粘度も低いため、高速度での塗布が可能になり床材、
壁材等の製造に好適である。
"Effects of the Invention" The viscosity of the plastisol prepared from the composition of the present invention is low not only in the low shear rate region but also in the high shear rate region, and the fluidity of the plastisol is excellent. It is particularly advantageous in the field of processing plastisols by method. For example, the low sol viscosity in the low shear rate range facilitates handling of the paste sol, e.g. feeding, filtration, and defoaming, and the low sol viscosity in the high shear rate range allows application at high speeds. flooring,
Suitable for manufacturing wall materials, etc.

さらに本発明の塩化ビニル系重合体組成物は一般式[I
]で表される燐酸エステル*たはその混合物を重合後の
ラテックスに添加して分散させた後に単に噴霧乾燥する
だけで得ることができ、経済的に、また捏業−ヒ極めて
有利である。
Furthermore, the vinyl chloride polymer composition of the present invention has the general formula [I
] or a mixture thereof can be obtained by simply adding and dispersing the phosphoric acid ester * or a mixture thereof to the polymerized latex and then spray-drying it, which is extremely advantageous economically and in terms of fabrication.

「実施例1 次に本発明を実施例にて更に詳述するが、本発明はその
要旨を越えない限り、以下の実施例によって限定される
ものではない。
Example 1 Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited by the following Examples unless the gist thereof is exceeded.

なお、実施例中に記載された「部」及び「%」は、重量
基準によった。
Note that "parts" and "%" described in the examples are based on weight.

また、テストに用いたプラスチゾルの配合は、次の通り
である。
The formulation of plastisol used in the test is as follows.

塩化ビニル系重合体組成物    100部7タル酸ノ
2−エチルヘキシル   70部炭酸カルシウム   
      150部Ca−Zn系安定剤      
    3部アゾ系発泡剤(アゾノカルボンアミド) 
5部希釈剤(ミネラルスピリット)    10部各テ
スト方法は以下の通りである。
Vinyl chloride polymer composition 100 parts 2-ethylhexyl 7-talate 70 parts calcium carbonate
150 parts Ca-Zn stabilizer
3-part azo blowing agent (azonocarbonamide)
5 parts diluent (mineral spirits) 10 parts Each test method is as follows.

B型精度(センチポイズ) BH型粘度計(東京計器製造所製)No、Gローターを
用い50rp−の回転数、23℃で測定した。
B-type precision (centipoise) Measurement was carried out using a BH-type viscometer (manufactured by Tokyo Keiki Seisakusho) No. G rotor at a rotational speed of 50 rpm and 23°C.

但し、上記配合系から安定剤を除いた配合物を用いた。However, a formulation was used in which the stabilizer was removed from the above formulation system.

BM型粘度(センチボイズ) BM型粘度計(東京計器!!!!遣所製)No、30−
ターを用い6 rpm、12rp槍の回転数、23℃で
測定した。
BM type viscosity (centiboise) BM type viscometer (manufactured by Tokyo Keiki!!!! Kensho) No. 30-
Measurements were made using a rotor at 6 rpm, 12 rp spear rotation speed, and 23°C.

〈実施例1、比較例1.2〉 撹拌機を備えた容積2O01の重合槽に脱イオン水80
kg、平均粒径0.5μの塩化ビニル重合体種子ラテッ
クス(乳化剤ニラウリル硫酸ナトリウム、重合開始剤:
 過硫酸カリウム−重亜硫酸ナトリウム系使用)を重合
体種子として4.f3kR仕込んだ後脱気して塩化ビニ
ル75.2kgを加えた。
<Example 1, Comparative Example 1.2> In a polymerization tank with a volume of 2001 equipped with a stirrer, 80 g of deionized water was added.
kg, vinyl chloride polymer seed latex with an average particle size of 0.5μ (emulsifier sodium nilauryl sulfate, polymerization initiator:
4. Using potassium persulfate-sodium bisulfite system) as a polymer seed. After charging f3kR, it was degassed and 75.2 kg of vinyl chloride was added.

温度を57℃に昇温した後、全量で0.05%(対塩化
ビニル)の過酸化水素−ホルムアルデヒドナトリウムス
ルホキシレートのレドックス開始剤を連続的に添加した
。更に、重合率が重合体種子と塩化ビニルの合計量の1
0%に達したときから不合の終わりまでの間乳化剤とし
てp−オクチルフェニルノオキシエチレン−3−スルホ
−2−ヒドロキシプロピルエーテルナトリウム塩を約8
%の水溶液として塩化ビニルに対して毎時0.08%の
割合で連続的に添加した。
After raising the temperature to 57°C, a redox initiator of hydrogen peroxide-sodium formaldehyde sulfoxylate in a total amount of 0.05% (based on vinyl chloride) was continuously added. Furthermore, the polymerization rate is 1 of the total amount of polymer seeds and vinyl chloride.
About 8% of p-octylphenylnooxyethylene-3-sulfo-2-hydroxypropyl ether sodium salt was added as an emulsifier from the time the concentration reached 0% until the end of the incorporation.
% aqueous solution at a rate of 0.08% per hour relative to vinyl chloride.

重合圧が57℃における塩化ビニルの飽和圧から1kg
/am”降下したときに重合を停正し、未反応モノマー
を回収した。得られたラテックス粒子の平均粒径は、0
.9μであった。該ラテックスを3分し、その2つにそ
れぞれ第1表に示す燐酸エステル混合物及びラウリル硫
酸ナトリウムを重合体当+)1.0%調整用乳化剤とし
て添加した後噴n乾燥し、次いで粉砕して塩化ビニル重
合体組成物を得た。
1kg from the saturation pressure of vinyl chloride at a polymerization pressure of 57℃
/am”, the polymerization was stopped and unreacted monomers were collected.The average particle size of the obtained latex particles was 0.
.. It was 9μ. The latex was divided into three parts, and a phosphoric acid ester mixture shown in Table 1 and sodium lauryl sulfate were added to each of the two parts as an emulsifier for adjusting 1.0% (per polymer), and then sprayed and dried, and then pulverized. A vinyl chloride polymer composition was obtained.

これらの塩化ビニル重合体組成物を用いで調製したプラ
スチゾルのゾル粘度を測定し、第1表に記載した。(第
1表は次頁) 〈実施例2、比較例3.4〉 実施例1において乳化剤としてラウリル硫酸ナトリウム
を、重合開始剤として過硫酸カリウム−メタ重亜硫酸ナ
トリウム系を用い、そして重合温度を50℃とした以外
は、全〈実施例1と同様にして塩化ビニル系重合体を得
た。これに、PIS2表に示す燐酸エステルもしくはド
デシルベンゼンスルホン酸ナトリウムを重合体当り0.
5%調整用乳化剤として添加した、塩化ビニル重合体組
成物を用いてプラスチゾルを調整した。得られたゾルの
粘度を第2表に示す。
The sol viscosities of plastisols prepared using these vinyl chloride polymer compositions were measured and are listed in Table 1. (Table 1 is on the next page) <Example 2, Comparative Example 3.4> In Example 1, sodium lauryl sulfate was used as the emulsifier, potassium persulfate-sodium metabisulfite system was used as the polymerization initiator, and the polymerization temperature was changed. A vinyl chloride polymer was obtained in the same manner as in Example 1 except that the temperature was 50°C. To this, phosphoric acid ester or sodium dodecylbenzenesulfonate shown in PIS 2 table was added at 0.0% per polymer.
Plastisols were prepared using a vinyl chloride polymer composition added as a 5% controlling emulsifier. The viscosity of the obtained sol is shown in Table 2.

〈実施例3〜6、比較例5〜9〉 撹拌機を備えた容積2O01の予備混合槽にイオン交換
水100に、、ラウロイルパーオキサイド600g、ラ
ウリル硫酸ナトリウム400g、ラウリルアルコール2
O0gを添加し次いで予備混合槽を脱気し塩化ビニル単
量体60kgを添加し攪拌しながら35℃に保持した。
<Examples 3 to 6, Comparative Examples 5 to 9> In a premixing tank with a volume of 2001 equipped with a stirrer, 100 g of ion-exchanged water, 600 g of lauroyl peroxide, 400 g of sodium lauryl sulfate, and 2 g of lauryl alcohol were added.
After adding Og, the premix tank was degassed, and 60 kg of vinyl chloride monomer was added, and the temperature was maintained at 35° C. with stirring.

均一に撹拌後孔化機を使用し所望の液滴径に分散しなが
ら予め脱気しておいた攪拌機を備えた容積2O01の反
応槽に移送した。分散液の移送完了後、反応槽の温度を
昇温し公知の方法で重合を行った。得られたラテックス
中の種子重合体粒子の平均径は0.5μであった。
After stirring uniformly, the mixture was dispersed into a desired droplet size using a porous machine and transferred to a reaction tank with a volume of 2001 equipped with a stirrer which had been previously degassed. After the transfer of the dispersion liquid was completed, the temperature of the reaction tank was raised and polymerization was carried out by a known method. The average diameter of the seed polymer particles in the obtained latex was 0.5μ.

上記のようにして調整した種子重合体を用いて重合を次
のように行った。
Polymerization was carried out as follows using the seed polymer prepared as described above.

攪拌機を備えた容積2O0 1の重合槽に脱イオン水8
0に、、種子重合体ラテックス5kg、炭酸水素ナトリ
ウム2Ogを仕込んだ後脱気して塩化ビニル単量体75
kgを仕込み、温度を50℃に昇温した後、予め溶解し
ておいた亜硫酸水素ナトリウムの0.3%水溶液を少量
ずづ重合槽へ連続的に添加し重合を開始した。亜硫酸水
素ナトリウムの添加開始後一定の反応速度で反応するよ
うに調整した。更に重合率が10%に達したときがら、
重合終了までの間、乳化剤として第3表に示す界面活性
剤を約8%の水溶液として塩化ビニル単量体に対して毎
時0.1%の割合で連続的に添加した。乳化剤全添加量
は塩化ビニルに対し0.6%であった。重合圧が50℃
における塩化ビニルの飽和圧から1 kg/ 0m2降
下したときに重合を停止し、未反応モノマーを回収した
。いずれの乳化剤によっても得られたラテックスの平均
粒径は1.0〜1.1μであり、ラテックスの安定性は
良好であった。得られたラテックスに表に示す調整用乳
化剤を加えて噴霧乾燥した後、粉砕して塩化ビニル系重
合体組成物を得た。この塩化ビニル系重合体組成物より
調整したプラスチゾルを上述のテスト方法により粘度を
測定した。結果を第3表に示す。
Deionized water 8 in a 200 1 volume polymerization tank equipped with a stirrer
0, 5 kg of seed polymer latex and 20 g of sodium bicarbonate were added, and then degassed to obtain 75% of vinyl chloride monomer.
kg was charged and the temperature was raised to 50° C., and then a 0.3% aqueous solution of sodium hydrogen sulfite, which had been dissolved in advance, was continuously added little by little to the polymerization tank to start polymerization. After the addition of sodium bisulfite was started, the reaction rate was adjusted to be constant. Furthermore, when the polymerization rate reached 10%,
Until the polymerization was completed, a surfactant shown in Table 3 as an emulsifier was continuously added as an approximately 8% aqueous solution at a rate of 0.1% per hour to the vinyl chloride monomer. The total amount of emulsifier added was 0.6% based on vinyl chloride. Polymerization pressure is 50℃
Polymerization was stopped when the vinyl chloride saturation pressure had dropped by 1 kg/0 m2 from the saturation pressure of vinyl chloride at , and unreacted monomers were collected. The average particle diameter of the latex obtained with any emulsifier was 1.0 to 1.1 μm, and the stability of the latex was good. The emulsifier for adjustment shown in the table was added to the obtained latex, the mixture was spray-dried, and then pulverized to obtain a vinyl chloride polymer composition. The viscosity of plastisol prepared from this vinyl chloride polymer composition was measured by the above-mentioned test method. The results are shown in Table 3.

手続補正書 昭和62年3月、2μ8 昭和62年特許顆第5572号 2 発明の名称 塩化ビニル系重合体組成物 3 補正をする者 事件との関係  特許出願人 名称 三菱化成ビニル株式会社 4代理人〒100 東京都千代田区丸の内二丁目5番2号 5 補正命令の日付  自発 6 補正により増加する発明のWLO 7補正の対象 明#II書の発明の詳細な説明の欄8 
補正の内容 (2)明#Il書!lS9頁第1行目、第15行目、及
ゾ第17行目に「調整」とあるをそれぞれ「調製」に訂
正する。
Procedural amendment March 1988, 2μ8 Patent No. 5572 of 1988 2 Name of the invention Vinyl chloride polymer composition 3 Relationship with the case of the person making the amendment Name of patent applicant Mitsubishi Kasei Vinyl Co., Ltd. 4 Agent 2-5-2-5 Marunouchi, Chiyoda-ku, Tokyo 100 Date of amendment order Spontaneous 6 WLO of inventions increased by amendment 7 Subject of amendment Column 8 for detailed explanation of the invention in Ming #II book
Contents of amendment (2) Ming #Il book! 1S page 9, lines 1, 15, and 17, the words ``adjustment'' are corrected to ``preparation.''

(3)明細書第12頁第17行目に「実施例1」とある
を「実施例1〜3」に訂正する。
(3) "Example 1" on page 12, line 17 of the specification is corrected to "Examples 1 to 3."

(4)明細書第12頁第17行目に[3分し、その2つ
に」とあるを「5分し、その4つに1に訂正する。
(4) In the 17th line of page 12 of the specification, the phrase ``divided into 3, then into 2'' is corrected to ``divided into 5, and then into 1 into 4.''

(5)明細書第12頁第19行目に[調整用乳化剤jと
あるをFrfR製用乳製剤乳化剤1する。
(5) On page 12, line 19 of the specification, "Adjusting emulsifier j" is used as FrfR emulsifier emulsifier 1.

(6)明細書第13頁第5行目に[実施例21とあるを
「実施例4〜6」に訂正する。
(6) On page 13, line 5 of the specification, [Example 21 is corrected to read "Examples 4 to 6."

(7)明細書第12頁第17行目及び第9行目に「実施
例1」とあるをそれぞれ「実施例1〜31に訂正する。
(7) "Example 1" in the 17th line and 9th line of page 12 of the specification is corrected to "Examples 1 to 31," respectively.

(8)明細書第12頁第17行目及び第14行目にrf
l19Jとあるをそれぞれ「11製」に訂正する。
(8) rf on page 12, line 17 and line 14 of the specification
Correct the text ``l19J'' to ``Made in 11.''

(9)明細書第14頁の第1表を以下の通りに補正する
(9) Table 1 on page 14 of the specification is amended as follows.

第   1    表 (10)明細書tj414頁のtI%2表を以下の通り
に補正する。
Table 1 (10) The tI%2 table on page 414 of the specification is amended as follows.

第    2    表 (11)明細書第15頁第1行目に「実施例3〜6、比
較例5〜9」とあるを[実施例7〜12、比較例5〜1
0」に訂正する。
Table 2 (11) In the first line of page 15 of the specification, "Examples 3 to 6, Comparative Examples 5 to 9" is replaced with [Examples 7 to 12, Comparative Examples 5 to 1]
Correct it to 0.

(12)明細書第16頁第14行目及び第17行目に[
調91とあるをそれぞれ「調製」に訂正する。
(12) On page 16, line 14 and line 17 of the specification [
Correct the words ``key 91'' to ``preparation.''

(13)明m書tPJ17頁全文を別紙の通りに補正す
る。
(13) The entire text of page 17 of the Memorandum of Understanding shall be amended as per the attached sheet.

Claims (2)

【特許請求の範囲】[Claims] (1)塩化ビニル系重合体100重量部に、一般式[
I ] (RO(CH_2CH_2O)n)kPO(OH)l(
OM)m・・・・・・[ I ] (式中、Rは炭素数8から30のアルキル基またはアル
キルフェニル基、 kは1から3の整数、 l及びmは0から2の整数で、k+l+m=3Mはアル
カリ金属原子、またはアンモニウム基、nは0から15
の整数 をそれぞれ示す。) で表されるリン酸エステルまたはその混合物を0.1〜
5重量部含有せしめた塩化ビニル系重合体組成物。
(1) 100 parts by weight of a vinyl chloride polymer was added with the general formula [
I] (RO(CH_2CH_2O)n)kPO(OH)l(
OM)m...[I] (wherein, R is an alkyl group or alkylphenyl group having 8 to 30 carbon atoms, k is an integer of 1 to 3, l and m are integers of 0 to 2, k+l+m=3M is an alkali metal atom or ammonium group, n is 0 to 15
Indicate each integer. ) Phosphate ester or mixture thereof represented by 0.1 to
A vinyl chloride polymer composition containing 5 parts by weight.
(2)一般式[ I ]で表されるリン酸エステルの混合
物が、Rがノニルフェニル基、m=0、n=9、であっ
て、k=1かつl=2、もしくは、k=2かつl=1で
あるものの混合物でその混合比(k=1:k=2)が1
:4〜4:1である特許請求の範囲第1項記載の塩化ビ
ニル系重合体組成物。
(2) A mixture of phosphoric esters represented by the general formula [I], where R is a nonylphenyl group, m=0, n=9, and k=1 and l=2, or k=2 and l=1, and the mixing ratio (k=1:k=2) is 1
The vinyl chloride polymer composition according to claim 1, wherein the polyvinyl chloride polymer composition has a ratio of:4 to 4:1.
JP557287A 1987-01-13 1987-01-13 Vinyl chloride based polymer composition Granted JPS63175057A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP557287A JPS63175057A (en) 1987-01-13 1987-01-13 Vinyl chloride based polymer composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP557287A JPS63175057A (en) 1987-01-13 1987-01-13 Vinyl chloride based polymer composition

Publications (2)

Publication Number Publication Date
JPS63175057A true JPS63175057A (en) 1988-07-19
JPH0547581B2 JPH0547581B2 (en) 1993-07-19

Family

ID=11614932

Family Applications (1)

Application Number Title Priority Date Filing Date
JP557287A Granted JPS63175057A (en) 1987-01-13 1987-01-13 Vinyl chloride based polymer composition

Country Status (1)

Country Link
JP (1) JPS63175057A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04226321A (en) * 1990-05-16 1992-08-17 Nippon Zeon Co Ltd Manufacture of window glass with gasket
JP2007297060A (en) * 2006-04-27 2007-11-15 Ajinomoto Co Inc Blister package for syringe
US20210198449A1 (en) * 2018-06-07 2021-07-01 Eastman Chemical Company Highly filled plastisols

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5391958A (en) * 1977-08-17 1978-08-12 Katsuta Kako Kk Stabilized halogeneecontaining resin composition
JPS588407A (en) * 1981-07-07 1983-01-18 Yokohama Rubber Co Ltd:The Pneumatic tire
JPS5876441A (en) * 1981-10-31 1983-05-09 Kanegafuchi Chem Ind Co Ltd Vinyl chloride pasty resin composition and vinyl chloride pasty resin sol composition
JPS5928227A (en) * 1982-08-09 1984-02-14 Victor Co Of Japan Ltd Magnetic recording medium
JPS59219378A (en) * 1983-05-27 1984-12-10 Shiraishi Chuo Kenkyusho:Kk Vinyl chloride resin paste sol composition
JPS60161451A (en) * 1984-01-30 1985-08-23 Sumitomo Chem Co Ltd Vinyl chloride based resin composition for powder molding
JPS60226542A (en) * 1984-04-25 1985-11-11 Mitsubishi Kasei Vinyl Co Flame-retardant vinyl chloride resin composition
JPS6116950A (en) * 1984-07-02 1986-01-24 Mitsubishi Kasei Vinyl Co Vinyl chloride resin film for agriculture
JPS6144939A (en) * 1984-08-10 1986-03-04 Mitsubishi Kasei Vinyl Co Vinyl chloride polymer composition
JPS61101544A (en) * 1984-10-25 1986-05-20 Sakai Chem Ind Co Ltd Chlorine-containing resin composition

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5391958A (en) * 1977-08-17 1978-08-12 Katsuta Kako Kk Stabilized halogeneecontaining resin composition
JPS588407A (en) * 1981-07-07 1983-01-18 Yokohama Rubber Co Ltd:The Pneumatic tire
JPS5876441A (en) * 1981-10-31 1983-05-09 Kanegafuchi Chem Ind Co Ltd Vinyl chloride pasty resin composition and vinyl chloride pasty resin sol composition
JPS5928227A (en) * 1982-08-09 1984-02-14 Victor Co Of Japan Ltd Magnetic recording medium
JPS59219378A (en) * 1983-05-27 1984-12-10 Shiraishi Chuo Kenkyusho:Kk Vinyl chloride resin paste sol composition
JPS60161451A (en) * 1984-01-30 1985-08-23 Sumitomo Chem Co Ltd Vinyl chloride based resin composition for powder molding
JPS60226542A (en) * 1984-04-25 1985-11-11 Mitsubishi Kasei Vinyl Co Flame-retardant vinyl chloride resin composition
JPS6116950A (en) * 1984-07-02 1986-01-24 Mitsubishi Kasei Vinyl Co Vinyl chloride resin film for agriculture
JPS6144939A (en) * 1984-08-10 1986-03-04 Mitsubishi Kasei Vinyl Co Vinyl chloride polymer composition
JPS61101544A (en) * 1984-10-25 1986-05-20 Sakai Chem Ind Co Ltd Chlorine-containing resin composition

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04226321A (en) * 1990-05-16 1992-08-17 Nippon Zeon Co Ltd Manufacture of window glass with gasket
JP2007297060A (en) * 2006-04-27 2007-11-15 Ajinomoto Co Inc Blister package for syringe
US20210198449A1 (en) * 2018-06-07 2021-07-01 Eastman Chemical Company Highly filled plastisols

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