JPH0242375B2 - - Google Patents
Info
- Publication number
- JPH0242375B2 JPH0242375B2 JP60160953A JP16095385A JPH0242375B2 JP H0242375 B2 JPH0242375 B2 JP H0242375B2 JP 60160953 A JP60160953 A JP 60160953A JP 16095385 A JP16095385 A JP 16095385A JP H0242375 B2 JPH0242375 B2 JP H0242375B2
- Authority
- JP
- Japan
- Prior art keywords
- melting point
- zinc
- resin
- granulation
- mixture
- 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 - Lifetime
Links
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- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は樹脂添加剤として好適な新規粒状物に
関する。
従来から粉末状の樹脂添加剤は取扱い上、粉塵
飛散による衛生上の問題、自動計量が困難である
という作業性の問題等種々欠点があるため、これ
らを粒状化する試みがなされ種々の方法が提案さ
れている。
一般に粉状の樹脂添加剤としては無機鉛化合
物,金属石鹸,酸化防止剤,紫外線吸収剤,滑
剤,有機りん酸化合物等々がある。
しかし従来の造粒品は粉塵防止,自動計量とい
う物理的改善を主たる目的としていたため、実際
に樹脂へ添加したとき、樹脂への分散性等で問題
があつた。特に或る種の化合物は粉状のままでは
物理的問題以外に分散性が非常に問題であつた。
本発明者らは上記問題のある特定の成分を選択
することにより、上記物理的問題改善以外に樹脂
への分散性が良好な粒状物を見出したのである。
すなわち本発明の粒状物としては
一般式
および
の混合物の1種以上と金属石鹸あるいは滑剤から
選ばれる1種以上を含有する平径粒径100μm〜
2000μmの粒状物である。
(但しRは炭素数10〜22のアルキル基,アルケニ
ル基、MはZn,Ba,Mg,Ca,Sr)
上記[],[]の混合物を選択した理由は、
該化合物は樹脂添加剤として汎用されるものであ
り、熱安定性,耐候性,加工性等に優れた効果を
発揮する化合物であると同時に粉状のままでは非
常に分散性に問題があつたのである。
又、金属石鹸、滑剤はしばしば[],[]の
混合物と併用されるためであると同時に、殆どの
金属石鹸、滑剤は[],[]の混合物よりも融
点(液状化温度)が低いため、[],[]の混
合物と混合して造粒した粒状品は、粒状品として
の融点(液状化温度)が下がり、融点(液状化温
度)の低い成分の融点で全体が軟化あるいは溶融
する特徴がある。
平均粒径を100μm〜2000μmとした理由は、
100μ以下では粉塵防止効果,自動計量性が充分
でなく、2000μm以上では樹脂の加工時間内で完
全に融けきらないため、分散不良を起こすからで
ある。
本発明で用いる造粒方法は特に制限はなく、従
来公知の噴霧造粒法,破砕造粒法等が採用出来る
が、特に急速混合機、即ち急速に回転する(約
500rpm以上)ロータを備えた粉体混合機を用い
て造粒する方法が好適である。得られた粒状品は
篩分し、所定の粒径のものに調節することが出来
る。[],[]の混合物と金属石鹸あるいは滑
剤の比率は特に制限はないが、通常1〜10対10〜
1で造粒するのが、作業性,分散性のうえから好
ましい。
本発明で用いられる一般式
および
で表される化合物としては以下の如きものが挙げ
られる。
等である。
次に本発明で用いられる金属石鹸としては以下
の如きものが挙げられる。
ステアリン酸亜鉛,オレイン酸亜鉛,パルミチ
ン酸亜鉛,ミスチリン酸亜鉛,ラウリン酸亜鉛,
ベヘニン酸亜鉛,12―ヒドロキシステアリン酸亜
塩,ステアリン酸カルシウム,パルミチン酸カル
シウム,ラウリン酸カルシウム,ステアリン酸マ
グネシウム等である。滑剤としては以下の如きも
のが挙げられる。ステアリン酸,パルミチン酸,
ベヘニン酸,メチレンビスステアリルアマイド,
エチレンビスステアリルアマイド,ステアリン酸
アマイド,ステアリルモノグリセライド,ステア
リルアルコール,セチルアルコール,ジペンタエ
リスリトールヘキサステアレート,ソルビタンモ
ノパルミテート,ポリオキシエチレンソルビタン
モノステアレート,トリステアリルリン酸,ジス
テアリルリン酸,ジステアリルペンタエリスリト
ールジホスフアイト,テトラステアリル水添ビス
フエノールAジホスフアイト等である。なお本発
明による粒状物には、分散性に影響を及ぼさない
範囲で、上記成分以外の成分が適宜含有されても
何ら差し使えはない。又、該粒状物は熱可塑性,
熱硬化性を問わず、種々の樹脂に目的,用途に応
じて他の成分と併用して添加される。樹脂として
は例えば、ポリ塩化ビニル,ポリ塩化ビニリデ
ン,塩素化ポリエチレン,塩化ビニル―酢酸ビニ
ル共重合体,等の塩素含有樹脂,ポリエステル樹
脂,ポリエチレン樹脂,ポリプロピレン樹脂,ポ
リスチレン樹脂,ポリカーボネート樹脂,ABS
樹脂,EVA樹脂アクリル樹脂,酢酸ビニル樹脂,
合成ゴム等である。以下実施例(粒状化例,配合
使用例)により説明する。
粒状化例 1
ジステアリルリン酸亜鉛とモノステアリルリン
酸亜鉛の混合粉状物(重量比1:1.4、融点[液
状化温度]185〜188℃、カサ9.7ml/g)2Kgを
201のスーパーミキサーに仕込み、2000rpmで20
分間急速撹拌し、次いで500rpmで5分間整粒し
た。冷却後20メツシユから100メツシユのふるい
で分級し、表1の粒状物No.1を得た。融点(液状
化温度)184〜187℃、カサ1.8ml/g平均粒子径
260μmであつた。
粒状化例 2
粒状化例1で使用したジステアリルリン酸亜鉛
とモノステアリルリン酸亜鉛の混合粉状物1Kg
と、ステアリン酸亜鉛(ステアリン酸と亜鉛華か
ら乾式法で合成し粉砕したもの)1Kgを201のス
ーパーミキサーに仕込み、2000rpmで15分間急速
撹拌し、次いで500rpmで5分間整粒した。冷却
後20メツシユから100メツシユのふるいで分級し、
表1の粒状物No.3を得た。融点(液状化温度)
122〜125℃、カサ2.0ml/g、平均粒子径320μm
であつた。
粒状化例 3
粒状化例1で使用したジステアリルリン酸亜鉛
とモノステアリルリン酸亜鉛の混合粉状物1Kg
と、メチレンビスステアリルアマイド1Kgを201
のスーパーミキサーに仕込み、1700rpmで20分間
急速撹拌し、次いで500rpmで5分間整粒した。
冷却後20メツシユから100メツシユのふるいで分
級し、表1の粒状物No.6を得た。融点(液状化温
度)143〜145℃、カサ1.7ml/g、平均粒子径
310μmであつた。
同様の方法により表1の粒状物を作成した。
The present invention relates to a novel particulate material suitable as a resin additive. Conventionally, powdered resin additives have various drawbacks such as hygiene problems due to dust scattering, workability problems such as difficulty in automatic measurement, etc., so attempts have been made to granulate them, and various methods have been developed. Proposed. Generally, powdered resin additives include inorganic lead compounds, metal soaps, antioxidants, ultraviolet absorbers, lubricants, and organic phosphoric acid compounds. However, since the main purpose of conventional granulated products was physical improvements such as dust prevention and automatic metering, there were problems with dispersibility in the resin when they were actually added to the resin. In particular, when some compounds are in powder form, dispersibility is a serious problem in addition to physical problems. By selecting a specific component with the above-mentioned problem, the present inventors have found a granular material that not only improves the above-mentioned physical problem but also has good dispersibility in resin. That is, the granular material of the present invention has the general formula and containing one or more of the mixtures thereof and one or more selected from metal soaps or lubricants with a diameter of 100 μm or more
It is a granular material of 2000μm. (However, R is an alkyl group or alkenyl group having 10 to 22 carbon atoms, and M is Zn, Ba, Mg, Ca, or Sr.) The reason for selecting the mixture of [] and [] above is as follows.
This compound is commonly used as a resin additive, and while it is a compound that exhibits excellent effects on heat stability, weather resistance, and processability, it also has problems with dispersibility when it is in powder form. It is. Also, this is because metal soaps and lubricants are often used in combination with mixtures of [] and [], and at the same time, most metal soaps and lubricants have a lower melting point (liquefaction temperature) than mixtures of [] and []. The melting point (liquefaction temperature) of the granular product granulated by mixing with the mixture of , [], [] decreases, and the entire product softens or melts at the melting point of the component with a lower melting point (liquefaction temperature). It has characteristics. The reason why the average particle size was set to 100 μm to 2000 μm is because
If it is less than 100 μm, the dust prevention effect and automatic metering performance will not be sufficient, and if it is more than 2000 μm, it will not be completely melted within the processing time of the resin, resulting in poor dispersion. The granulation method used in the present invention is not particularly limited, and conventionally known spray granulation methods, crushing granulation methods, etc. can be adopted, but in particular, a rapid mixer, that is, a rapidly rotating (approximately
A method of granulation using a powder mixer equipped with a rotor (at least 500 rpm) is suitable. The obtained granular product can be sieved and adjusted to a predetermined particle size. There is no particular restriction on the ratio of the mixture [], [] to the metal soap or lubricant, but it is usually 1-10:10-10.
It is preferable to granulate with No. 1 from the viewpoint of workability and dispersibility. General formula used in the present invention and Examples of the compound represented by the above include the following. etc. Next, the metal soaps used in the present invention include the following. Zinc stearate, zinc oleate, zinc palmitate, zinc mystilate, zinc laurate,
These include zinc behenate, subsalt 12-hydroxystearate, calcium stearate, calcium palmitate, calcium laurate, and magnesium stearate. Examples of lubricants include the following. stearic acid, palmitic acid,
Behenic acid, methylene bisstearylamide,
Ethylene bisstearylamide, stearamide, stearyl monoglyceride, stearyl alcohol, cetyl alcohol, dipentaerythritol hexastearate, sorbitan monopalmitate, polyoxyethylene sorbitan monostearate, tristearyl phosphate, distearyl phosphate, distearyl These include pentaerythritol diphosphite, tetrastearyl hydrogenated bisphenol A diphosphite, and the like. It should be noted that the granules according to the present invention may contain components other than the above-mentioned components, as long as the dispersibility is not affected. Moreover, the granules are thermoplastic,
Regardless of thermosetting properties, it is added to various resins in combination with other components depending on the purpose and use. Examples of resins include chlorine-containing resins such as polyvinyl chloride, polyvinylidene chloride, chlorinated polyethylene, vinyl chloride-vinyl acetate copolymers, polyester resins, polyethylene resins, polypropylene resins, polystyrene resins, polycarbonate resins, and ABS.
Resin, EVA resin acrylic resin, vinyl acetate resin,
Synthetic rubber, etc. This will be explained below using examples (granulation examples, blending usage examples). Granulation example 1 2 kg of mixed powder of zinc distearyl phosphate and zinc monostearyl phosphate (weight ratio 1:1.4, melting point [liquefaction temperature] 185-188°C, bulk 9.7 ml/g)
201 super mixer, 2000rpm
The mixture was rapidly stirred for a minute and then sized at 500 rpm for 5 minutes. After cooling, the mixture was classified using a 20 to 100 mesh sieve to obtain granular material No. 1 shown in Table 1. Melting point (liquefaction temperature) 184-187℃, bulk 1.8ml/g average particle diameter
It was 260μm. Granulation example 2 1 kg of mixed powder of zinc distearyl phosphate and zinc monostearyl phosphate used in granulation example 1
and 1 kg of zinc stearate (synthesized and pulverized from stearic acid and zinc white using a dry method) were placed in a 201 super mixer, rapidly stirred at 2000 rpm for 15 minutes, and then sized at 500 rpm for 5 minutes. After cooling, it is classified using a 20 mesh to 100 mesh sieve.
Granular material No. 3 shown in Table 1 was obtained. Melting point (liquefaction temperature)
122-125℃, bulk 2.0ml/g, average particle size 320μm
It was hot. Granulation Example 3 1Kg of mixed powder of zinc distearyl phosphate and zinc monostearyl phosphate used in Granulation Example 1
and 1Kg of methylene bisstearylamide at 201
The mixture was charged into a super mixer, rapidly stirred at 1700 rpm for 20 minutes, and then sized at 500 rpm for 5 minutes.
After cooling, the mixture was classified using a 20 to 100 mesh sieve to obtain granular material No. 6 shown in Table 1. Melting point (liquefaction temperature) 143-145℃, bulk 1.7ml/g, average particle size
It was 310μm. The granules shown in Table 1 were prepared in a similar manner.
【表】【table】
【表】
配合使用例 1
表2の配合物を150℃のロールにて混練し、添
加物が完全にフイルム中に分散し、未分散粒子が
無くなるまでの時間を示した。[Table] Formulation Example 1 The formulation shown in Table 2 was kneaded with a roll at 150°C, and the time required for the additive to be completely dispersed in the film and for there to be no undispersed particles is shown.
【表】【table】
【表】
※1 粒状化例1で使用した粉状物
配合使用例 2
表3の配合物を170℃のロールにて5分間混練
し、添加物の分散状態を肉眼で観察し評価した。[Table] *1 Example of using the powder blend used in Granulation Example 1 2 The blend in Table 3 was kneaded for 5 minutes with a roll at 170°C, and the dispersion state of the additive was observed and evaluated with the naked eye.
【表】【table】
Claims (1)
選ばれる1種以上を含有する平均粒径100μm〜
2000μmの粒状物。 (但しRは炭素数10〜22のアルキル基,アルケニ
ル基、MはZn,Ba,Mg,Ca,Sr) 2 金属石鹸あるいは滑剤の融点が一般式[]
と[]の混合物の融点よりも低いことを特徴と
する特許請求の範囲第1項記載の粒状物。[Claims] 1. General formula and containing one or more of the mixtures thereof and one or more selected from metal soaps or lubricants with an average particle size of 100 μm or more
2000μm granules. (However, R is an alkyl group or alkenyl group having 10 to 22 carbon atoms, M is Zn, Ba, Mg, Ca, Sr) 2 The melting point of the metal soap or lubricant is the general formula []
The granular material according to claim 1, which has a melting point lower than the melting point of the mixture of and [ ].
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16095385A JPS6220538A (en) | 1985-07-19 | 1985-07-19 | Granules |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16095385A JPS6220538A (en) | 1985-07-19 | 1985-07-19 | Granules |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6220538A JPS6220538A (en) | 1987-01-29 |
| JPH0242375B2 true JPH0242375B2 (en) | 1990-09-21 |
Family
ID=15725765
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16095385A Granted JPS6220538A (en) | 1985-07-19 | 1985-07-19 | Granules |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6220538A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009031680A1 (en) | 2007-09-07 | 2009-03-12 | The Nisshin Oillio Group, Ltd. | Method for separation of 1,3-disaturated-2-unsaturated triglyceride |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0719824B1 (en) * | 1994-12-28 | 2001-06-27 | Ciba SC Holding AG | Low-dust granules of plastic additives |
| JP4640753B2 (en) * | 2003-12-08 | 2011-03-02 | 株式会社Adeka | Vinyl chloride resin composition |
| JP5286683B2 (en) * | 2007-03-23 | 2013-09-11 | 住友化学株式会社 | Phosphite-containing granular composition and method for producing the same |
| DE102008053629B4 (en) * | 2008-10-29 | 2012-09-06 | Baerlocher Gmbh | Glycerine ether-containing stabilizer composition for halogen-containing polymers, and their use |
| CN115960420A (en) * | 2022-12-27 | 2023-04-14 | 广东圆融新材料有限公司 | High-heat-resistance high-haze plate, preparation method and application |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5926632B2 (en) * | 1976-12-18 | 1984-06-29 | 堺化学工業株式会社 | Method for producing organophosphorus compounds |
| JPS54102348A (en) * | 1978-01-31 | 1979-08-11 | Adeka Argus Chem Co Ltd | Halogen-containing resin composition |
| JPS5630452A (en) * | 1979-08-21 | 1981-03-27 | Adeka Argus Chem Co Ltd | Halogen-containing resin composition |
| FR2473618A1 (en) * | 1980-01-11 | 1981-07-17 | Geostock | PROCESS FOR PRODUCING UNDERGROUND FLUID STORAGE |
-
1985
- 1985-07-19 JP JP16095385A patent/JPS6220538A/en active Granted
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009031680A1 (en) | 2007-09-07 | 2009-03-12 | The Nisshin Oillio Group, Ltd. | Method for separation of 1,3-disaturated-2-unsaturated triglyceride |
| EP2388306A1 (en) | 2007-09-07 | 2011-11-23 | The Nisshin OilliO Group, Ltd. | Fractionation method of 1,3-disaturated-2-unsaturated triglyceride |
| EP2388307A1 (en) | 2007-09-07 | 2011-11-23 | The Nisshin OilliO Group, Ltd. | Fractionation method of 1,3-disaturated-2-unsaturated triglyceride |
| EP2399977A1 (en) | 2007-09-07 | 2011-12-28 | The Nisshin OilliO Group, Ltd. | Fractionation method of 1,3-disaturated-2-unsaturated triglyceride |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6220538A (en) | 1987-01-29 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| EXPY | Cancellation because of completion of term |