JPS6220538A - Granules - Google Patents
GranulesInfo
- Publication number
- JPS6220538A JPS6220538A JP16095385A JP16095385A JPS6220538A JP S6220538 A JPS6220538 A JP S6220538A JP 16095385 A JP16095385 A JP 16095385A JP 16095385 A JP16095385 A JP 16095385A JP S6220538 A JPS6220538 A JP S6220538A
- Authority
- JP
- Japan
- Prior art keywords
- melting point
- resin
- granules
- zinc
- lubricant
- 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
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は樹脂添加剤として好適な新現粒吠物に関する。[Detailed description of the invention] The present invention relates to a new granule suitable as a resin additive.
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、自動計量が円錐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。Traditionally, powdered resin additives have had various drawbacks such as hygiene problems due to dust scattering and workability problems due to the conical shape of automatic metering, so attempts have been made to granulate them, and various methods have been developed. Proposed.
一般に粉状の樹脂添加剤としては無機鉛化合物。Inorganic lead compounds are generally used as powdered resin additives.
金属石鹸、酸化防止剤、紫外線吸収剤、滑剤、°イ1機
りん酸化合物等々がある。These include metal soaps, antioxidants, ultraviolet absorbers, lubricants, and phosphoric acid compounds.
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、檜脂への分散性等で問題があった。特に成る種
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
常に間圧であった。However, since the main purpose of conventional granulated products was physical improvements such as dust prevention and automatic metering, when they were actually added to resins, there were problems with dispersibility in cypress fat. In addition to physical problems, the dispersibility of certain types of compounds in powder form was extremely poor.
本発明者らは上記間江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。By selecting a certain specific component of the above-mentioned material, the present inventors have discovered a granular material that not only improves the above-mentioned physical problems but also has good dispersibility in resins.
すなわち本発明の粒状物としては
一般式
%式%)
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均粒径100μm〜2000μ
mの粒状物である。That is, the granules of the present invention contain one or more of the mixtures of the general formula (%) and one or more selected from metal soaps or lubricants, and have an average particle diameter of 100 μm to 2000 μm.
It is a granular material of m.
(イロしRは炭素V110〜22のアルキル基、アルケ
ニル基、MはZn、Da、Mg、Ca、Sr)上記[1
]、[II]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、耐臥
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ったのであ
る。(Iroshi R is an alkyl group or alkenyl group having carbon V110 to 22, M is Zn, Da, Mg, Ca, Sr) Above [1
], [II] was selected because this compound is widely used as a resin additive, and it is a compound that exhibits excellent effects on heat stability, aging resistance, processability, etc. If it remained in powder form, there were problems with dispersibility.
又、金属石鹸、滑剤はしばしば[11,[11]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[1]、 [II]の混合物よりも融点(液状
化温度)が低いため、[I]、[II]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。Also, because metal soaps and lubricants are often used in combination with mixtures of [11, [11], most metal soaps and
Since the lubricant has a lower melting point (liquefaction temperature) than the mixture of [1] and [II], the granular product granulated by mixing with the mixture of [I] and [II] has a lower melting point (liquefaction temperature) than the mixture of [I] and [II]. liquefaction temperature), and the entire product softens or melts at the melting point of the component with a low melting point (liquefaction temperature).
平均粒径を100μm〜2000μmとした理由は、1
00 /A以下では粉塵防止効果、自動針l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。The reason for setting the average particle size to 100 μm to 2000 μm is 1.
If it is less than 00/A, the dust prevention effect and automatic needleability 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.
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。[:I] [nl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2分散性のうえ
から好ましい。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 rotor that rotates rapidly (about 500 rpm or more) is used. A method of granulation using a powder mixer is preferred. The obtained granular product can be sieved and adjusted to a predetermined particle size. [:I] [The ratio of the mixture of nl and the metal soap or lubricant is not particularly limited, but it is usually 1-
It is preferable to granulate at a ratio of 10:10-1 from the viewpoint of workability and 2-dispersibility.
本発明で用いられる一般式 %式% [] で表される化合物としては以下の如さものが挙げO0 等である。General formula used in the present invention %formula% [] Examples of compounds represented by O0 include the following: etc.
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。Next, the metal soaps used in the present invention include the following.
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。These include zinc stearate, zinc oleate, zinc palmitate, zinc mystilate, zinc laurate, zinc behenate, subsalt 12-hydroxystearate, calcium stearate, calcium palmitate, calcium laurate, and magnesium stearate. Examples of lubricants include the following. stearic acid, palmitic acid.
ヘヘニン酸、メチレンビスステアリルアマイド。Hehenic acid, methylene bisstearylamide.
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、スデアリルモノグリセライト、ステアリルアルコー
ル、七チルアルコール、ジペンタエリスリトールへキザ
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ァイト、テトラステアリル水添ビ
スフェノールAジホスアイト等である。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。Ethylene bisstearylamide, stearamide, sudearyl monoglycerite, stearyl alcohol, heptyl alcohol, dipentaerythritol hexastearate, sorbitan monopalmitate, polyoxyethylene sorbitan monostearate, tristearyl phosphate, di These include stearyl phosphoric acid, distearyl 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 added to various resins, whether thermoplastic or thermosetting, in combination with other components depending on the purpose and use. Examples of the resin include polyvinyl chloride and polyvinylidene chloride.
塩素化ポリエチレン、塩化ビニル−酢酸ビニル共重合体
9等の塩素含有樹脂、ポリエステル樹脂。Chlorine-containing resins such as chlorinated polyethylene, vinyl chloride-vinyl acetate copolymer 9, and polyester resins.
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、AIDS樹脂。Polyethylene resin, polypropylene resin, polystyrene resin, polycarbonate resin, AIDS resin.
EVA樹脂アクリル樹脂、酢酸ビニル樹脂1舎成ゴム等
である。以下実施例(粒状化例、配合使用例)により説
明する。EVA resin, acrylic resin, vinyl acetate resin, synthetic rubber, etc. This will be explained below using Examples (granulation examples, blending usage examples).
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[液状化温度コ
185〜188℃、カサ9.7ml/g)2kgを20
1のスーパーミキサーに仕込み、200Orpmで、2
0分間急速撹拌し、次いて500rpmで5分間整粒し
た。冷却後20メツシユから100メツシユのふるいて
分級し、表1の粒状物No、1を得た。融点(液状化温
度)1[1/L〜187℃、カサ1.8ml/g平均粒
子径26071 mであった。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) 20
Pour into super mixer No. 1 and mix at 200 rpm, No. 2
The mixture was rapidly stirred for 0 minutes, and then sized at 500 rpm for 5 minutes. After cooling, the mixture was sieved and classified into 20 to 100 meshes to obtain granules No. 1 shown in Table 1. The melting point (liquefaction temperature) was 1 [1/L to 187°C, the bulk was 1.8 ml/g, and the average particle diameter was 26071 m.
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ンH合粉状物1 k g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、200Orpm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であった。Granulation Example 2 1 kg of the mixed powder of zinc distearyl phosphate and zinc monostearyl phosphate used in Granulation Example 1 and zinc stearate (synthesized from stearic acid and zinc white by a dry method and pulverized) (1 kg) was placed in a 201 super mixer, rapidly stirred at 200 rpm for 15 minutes, and then sized at 500 rpm for 5 minutes. After cooling, it was classified using a 20 mesh to 100 mesh sieve, and the granular material No. in Table 1 was classified.
, got 3. The melting point (liquefaction temperature) was 122 to 125°C, the bulk was 2.0 ml/g, and the average particle diameter was 320 μm.
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11(gを201のスーパーミキ
サーに仕込み、1700 r pmで20分間急速撹拌
し、次いて500 rpmで5分間整粒した。冷却後2
0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、Gを得た。融点(液状化温度)143〜
145℃、カサ1.7ml/g、平均粒子径310μm
であった。Granulation Example 3 1 kg of the mixed powder of zinc distearyl phosphate and zinc monostearyl phosphate used in Granulation Example 1 and 11 g of methylene bisstearylamide were charged into a 201 super mixer, and 20 g was mixed at 1700 rpm. The mixture was rapidly stirred for 1 minute, and then sized at 500 rpm for 5 minutes.After cooling, 2
Classified with a sieve of 0 mesh to 100 mesh, Table 1
Granular materials No. G were obtained. Melting point (liquefaction temperature) 143~
145℃, bulk 1.7ml/g, average particle size 310μm
Met.
同様の方法により表1の粒状物を作成した。The granules shown in Table 1 were prepared in a similar manner.
(数値はffi量比を表す)
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
が完全にフィルム中に分散し、未分散粒子が無くなるま
での時間を示した。(The numerical value represents the ffi amount ratio) Compound usage example 1 The composition shown in Table 2 is 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. Ta.
※l 粒吠化例1て使用した粉状物
配合使用例2
表3の配合物を170°C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=f価した。*l Example 2 of using the powder mixture used in Granule Formation Example 1 The mixture in Table 3 was kneaded for 5 minutes with a roll at 170°C.
The dispersion state of the additive was visually observed and evaluated as an f value.
表3Table 3
Claims (1)
る1種以上を含有する平均粒径100μm〜2000μ
m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[ I ]と[II]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。(1) One or more mixtures of general formulas ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ [I] and ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ [II] and one or more selected from metal soaps or lubricants. Containing average particle size 100μm ~ 2000μm
m granules. (However, R is an alkyl group or alkenyl group having 10 to 22 carbon atoms, and M is Zn, Ba, Mg, Ca, or Sr.) (2) The melting point of the metal soap or lubricant is that of the mixture of general formulas [I] and [II]. The granular material according to claim 1, which has a melting point lower than the melting point.
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 true JPS6220538A (en) | 1987-01-29 |
JPH0242375B2 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 (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005056672A1 (en) * | 2003-12-08 | 2005-06-23 | Asahi Denka Co., Ltd. | Vinyl chloride resin composition |
JP2007314810A (en) * | 1994-12-28 | 2007-12-06 | Ciba Specialty Chem Holding Inc | Low-dust granule of plastic additive |
JP2008231353A (en) * | 2007-03-23 | 2008-10-02 | Sumitomo Chemical Co Ltd | Phosphite-containing granular composition and its manufacturing method |
DE102008053629A1 (en) * | 2008-10-29 | 2010-05-12 | Baerlocher Gmbh | Stabilizer composition, useful for stabilizing halogen containing polymers, comprises glycerol monoalkyl-ethers and organic or inorganic compound containing di- or tri- or tetravalent metal capable of forming salts with mineral acid |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI441915B (en) | 2007-09-07 | 2014-06-21 | Nisshin Oillio Group Ltd | Method of fractionating 1, 3-disaturated-2-unsaturated triglyceride |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5384919A (en) * | 1976-12-18 | 1978-07-26 | Sakai Chem Ind Co Ltd | Preparation of organic phosphorous compound |
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 |
JPS56101494A (en) * | 1980-01-11 | 1981-08-14 | Fr Do Sutotsukaajiyu Jieorojii | Improved under ground storing method of liquid |
-
1985
- 1985-07-19 JP JP16095385A patent/JPS6220538A/en active Granted
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5384919A (en) * | 1976-12-18 | 1978-07-26 | Sakai Chem Ind Co Ltd | Preparation of organic phosphorous compound |
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 |
JPS56101494A (en) * | 1980-01-11 | 1981-08-14 | Fr Do Sutotsukaajiyu Jieorojii | Improved under ground storing method of liquid |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007314810A (en) * | 1994-12-28 | 2007-12-06 | Ciba Specialty Chem Holding Inc | Low-dust granule of plastic additive |
WO2005056672A1 (en) * | 2003-12-08 | 2005-06-23 | Asahi Denka Co., Ltd. | Vinyl chloride resin composition |
JP2005170966A (en) * | 2003-12-08 | 2005-06-30 | Asahi Denka Kogyo Kk | Vinyl chloride resin composition |
JP4640753B2 (en) * | 2003-12-08 | 2011-03-02 | 株式会社Adeka | Vinyl chloride resin composition |
KR101109209B1 (en) | 2003-12-08 | 2012-01-30 | 가부시키가이샤 아데카 | Vinyl chloride resin composition |
JP2008231353A (en) * | 2007-03-23 | 2008-10-02 | Sumitomo Chemical Co Ltd | Phosphite-containing granular composition and its manufacturing method |
DE102008053629A1 (en) * | 2008-10-29 | 2010-05-12 | Baerlocher Gmbh | Stabilizer composition, useful for stabilizing halogen containing polymers, comprises glycerol monoalkyl-ethers and organic or inorganic compound containing di- or tri- or tetravalent metal capable of forming salts with mineral acid |
DE102008053629B4 (en) * | 2008-10-29 | 2012-09-06 | Baerlocher Gmbh | Glycerine ether-containing stabilizer composition for halogen-containing polymers, and their use |
Also Published As
Publication number | Publication date |
---|---|
JPH0242375B2 (en) | 1990-09-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0234529B1 (en) | A thermoplastic resin composition for cleaning | |
US4324709A (en) | Process for incorporating a modifier of properties of a shaped synthetic polymer containing a biodegradable substance therein, and the product of the process | |
US4675122A (en) | Combined antiblocking and lubricant concentrate | |
US5846656A (en) | Stabilization systems for polymeric material in pellet form | |
JPS6363752A (en) | Polymer concentrate and its production | |
US20090054698A1 (en) | Granular Polymer Additives and Their Preparation | |
JP2002220549A (en) | Granular inorganic filler and method for producing the same and resin composition compounded with the same | |
JPH05179056A (en) | Method for obtaining granular form of additive for organic high polymer | |
US3461081A (en) | Stabilizing agent for a halogen containing synthetic resin consisting of a basic inorganic acid salt of lead coated with a fatty acid soap of lead,cadmium or calcium | |
EP1115784B1 (en) | Low dust balanced hardness antioxidant pellets and process for the production of same | |
KR20000070720A (en) | Particulate Diacetal Composition, Process for Producing the Same, and Polyolefin Resin Composition and Molding | |
JPS6220538A (en) | Granules | |
US3755450A (en) | Free flowing uv absorber compositions with magnesium or zinc salts offatty acids | |
EP0233819A2 (en) | Animal feed supplement formulation | |
GB2029836A (en) | Plastics Based Composition | |
JPH0368638A (en) | Stabilized phosphite composition | |
JP2002512287A (en) | Granular compositions of anti-adhesives and additives for polymer production | |
JPH0768411B2 (en) | Method for producing powder-free metal-containing stabilizer particles and halogen-containing polymer stabilized with the particles | |
JPH06256763A (en) | Granular flame retardant composition | |
CA1065989A (en) | Polyolefin composition and method for minimizing migration of u.v. absorber therein | |
JPS6234060B2 (en) | ||
JP2001048992A (en) | Holding master batch composition and its production | |
US5543447A (en) | Stabilization of red amorphous phosphorus by ordered polymeric structures for the manufacture of non-emissive fire retardant plastics | |
JPH0570602A (en) | Production of vinyl chloride-based resin composition | |
JP3425768B2 (en) | Granulated antistatic agent and method of using the same |
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 |